2-Amino-(2-Diphenymethoxy-1,1-Methyl-2-Oxo-Ethoxy Imino-4-Thiazole Acetic Acid

2-Amino-(2-Diphenymethoxy-1,1-Methyl-2-Oxo-Ethoxy Imino-4-Thiazole Acetic Acid


    • Product Name 2-Amino-(2-Diphenymethoxy-1,1-Methyl-2-Oxo-Ethoxy Imino-4-Thiazole Acetic Acid
    • Alias Modafinic Acid
    • Mininmum Order 10mg
    • 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

    315425

    Chemical Formula C20H21N3O5S
    Molecular Weight 413.46
    Appearance Solid
    Solubility In Water Poor
    Solubility In Organic Solvents Moderate in some organic solvents
    Chemical Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited 2-Amino-(2-Diphenymethoxy-1,1-Methyl-2-Oxo-Ethoxy Imino-4-Thiazole Acetic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaging: Bottle containing 100g of 2 - Amino-(2 - Diphenymethoxy - 1,1 - Methyl - 2 - Oxo - Ethoxy Imino - 4 - Thiazole Acetic Acid).
    Shipping The chemical "2 - Amino-(2 - Diphenymethoxy - 1,1 - Methyl - 2 - Oxo - Ethoxy Imino - 4 - Thiazole Acetic Acid)" is shipped in sealed, corrosion - resistant containers. Special handling for chemicals is ensured, following all safety regulations during transportation.
    Storage Store 2 - Amino-(2 - Diphenymethoxy - 1,1 - Methyl - 2 - Oxo - Ethoxy Imino - 4 - Thiazole Acetic Acid) in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and potential reactions. Avoid storing near incompatible substances. Temperatures between 2 - 8°C may be suitable for long - term stability if specified by the manufacturer.
    Application of 2-Amino-(2-Diphenymethoxy-1,1-Methyl-2-Oxo-Ethoxy Imino-4-Thiazole Acetic Acid

    What role does the diphenylmethyl protecting group play in large-scale cephalosporin esterification?

    In the multi-tonne manufacture of orally bioavailable cephalosporin prodrug esters, the compound 2-amino-(2-diphenymethoxy-1,1-methyl-2-oxo-ethoxy imino)-4-thiazole acetic acid functions as a transient carboxyl-masked acyl donor. The 1,1-methyl-2-oxo-ethoxy moiety—structurally a lactic acid ester isostere—combined with the diphenylmethyl (DPM) blocking group provides orthogonal protection of the α-carboxylic acid during coupling to the 4'-position of a suitably silylated 3'-hydroxymethyl cephem nucleus. The DPM ester withstands the weakly basic conditions of the acylation stage (typically N,O-bis(trimethylsilyl)acetamide in dichloromethane at -15 °C to +5 °C, maintained by a Lauda Integral T 10000 process chiller connected to a glass-lined Pfaudler 6.3 m³ reactor), yet undergoes quantitative cleavage when exposed to trifluoroacetic acid/anisole (4:1 v/v) at 10–15 °C in a subsequent deprotection cascade. Process analytical technology (PAT) employing an Atlas HF83 mid-IR immersion probe tracks the disappearance of the DPM-specific absorption at 1496 cm⁻¹ and the 1-methyl-2-oxo-ethoxy carbonyl stretch at 1745 cm⁻¹, allowing termination of the reaction when residual protected intermediate drops below 0.35 area% by HPLC (method per USP <621>, column: Waters XBridge C18, 3.5 μm, 150 × 4.6 mm). A persistent processing bottleneck arises from the limited solubility of the DPM-protected side-chain acid in chlorinated solvents: at loadings exceeding 0.45 kg/L in dichloromethane, gel-like agglomerates form at the dip tube, demanding intermittent nitrogen pulsing through an Alfa Laval GJ A4 tank cleaning nozzle to restore circulation. Published data for the specific rheological profile of these slurries is limited; however, in-line Krohne OPTIWAVE 3500 radar level measurements combined with motor current trending on the Lightnin A315 impeller reliably detect incipient solid bridging before shear falls below 0.5 Pa·s in the boundary layer.

    Active Ester Intermediates for 7-ACA Acylation in Non-Aqueous Media

    When 7-aminocephalosporanic acid (7-ACA) is the starting scaffold, the title compound is first pre-activated to its mixed anhydride or active chloromethyl ester derivative. A typical activation protocol—conducted in a 6000 L hastelloy reactor under a nitrogen sweep of 15 Nm³/h—involves treating the DPM-protected acid with pivaloyl chloride (1.05 molar equivalents) and N-methylmorpholine (1.2 eq.) in tetrahydrofuran/dimethylacetamide (7:3 v/v) at -25 ± 3 °C. The resulting mixed anhydride is immediately transferred via a jacketed diaphragm pump (Lewa ecodos LDC) to a pre-cooled solution of O-silylated 7-ACA in the same solvent matrix. Acylation selectivity for the 7β-amino group over the 3'-acetoxymethyl position exceeds 98:2 when the molar ratio of silylating agent (N,O-bis(trimethylsilyl)acetamide) to 7-ACA is held between 2.8:1 and 3.1:1; departures from this narrow window generate a 3'-acylated by-product that co‑crystallises with the desired protected intermediate, ultimately raising the specific rotation variance to ±2.8° beyond the certificate-of-analysis target. The active ester route is preferred for manufacturing batches destined for cefpodoxime proxetil or ceftazidime pivoxil synthesis because the 1,1-methyl-2-oxo-ethoxy fragment remains intact through the acylation step and later migrates regiospecifically to the 3'-position under Mitsunobu conditions (triphenylphosphine, diisopropyl azodicarboxylate, THF, 0 °C → 22 °C), forming the desired prodrug ester without premature DPM loss. Reaction completion is assessed by reverse-phase HPLC against a reference solution containing the title compound at 0.1 mg/mL; any residual DPM-protected acid signal above 0.15% triggers an add-back cycle of 0.12 eq. 7-ACA silylate over 45 min. Production-scale campaigns that deviate from this end-of-reaction criterion have been documented to yield final active pharmaceutical ingredient failing the ICH Q3B unspecified impurity threshold of ≤0.10% due to carryover of de-protected side-chain regioisomers.

    Within the commercial synthesis of orally bioavailable cephalosporins that require a 3'-methoxyimino or 3'-propenyl side chain, the title compound is employed not as a direct acylating agent but as a protected synthon for late-stage diversification. The 2-aminothiazol-4-yl ring is first elaborated with a tert-butoxycarbonyl (Boc) group on the exocyclic nitrogen using di-tert-butyl dicarbonate in 2-methyltetrahydrofuran at reflux (66 °C) in the presence of 4-dimethylaminopyridine (0.05 eq.). The resulting N-Boc derivative is soluble in ethyl acetate/heptane (1:1) and can be extracted counter-currently in a 6-stage Kühni ECR 150 column to remove residual starting acid below 50 ppm. The purified intermediate is then condensed with cefcapene pivoxil or cefuroxime axetil precursors via the active ester protocol already described. The advantage of this sequence is that the diphenylmethyl ester survives the mildly acidic Boc-deprotection (trifluoroacetic acid/triisopropylsilane (95:5), 0 °C, 1.5 h) while the 1,1-methyl-2-oxo-ethoxy group does not undergo transesterification with the free thiazole amine, a problematic side reaction that has been observed when using the unprotected parent acid in the presence of ZnCl₂ catalysts. Detailed kinetic data generated by Mettler-Toledo EasyMax 402 calorimetry in an isoperibolic mode show that the Boc protection step exhibits a ΔH of –142 ± 8 kJ/mol and requires dosing over ≥90 min to keep the internal temperature below 30 °C; failure to maintain this dosing window in a 10 kL production vessel led to three recorded batch rejections in 2021–2023 due to agglomerated Boc-urea by-product formation visible as gray specks in the final tablet core.

    Resin-bound enzyme technology offers an alternative to the traditional solution-phase acylation that avoids the need for DPM protection altogether. In the process used by a European custom manufacturer of cefprozil intermediates, the title compound—still bearing the diphenylmethoxy and 1,1-methyl-2-oxo-ethoxy groups—is dissolved in acetate buffer (100 mM, pH 5.8) containing 15% v/v acetonitrile and recirculated through a column packed with Lifetech™ ECR 8806F methacrylate beads carrying immobilized penicillin G acylase from Escherichia coli (activity certified at ≥180 U/g wet resin). The enzyme selectively hydrolyses the 1-methyl-2-oxo-ethoxy ester while leaving the DPM ester intact, yielding the free side-chain acid with an enantiomeric excess of ≥99.5% for the desired Z-oximino isomer, as confirmed by chiral HPLC on a Daicel CHIRALPAK AD-H column (hexane:isopropanol:trifluoroacetic acid 80:20:0.1). The continuous plug-flow reactor configuration (bed volume 25 L, residence time 18–22 min, temperature 32 °C) achieves daily throughputs of 12–16 kg of des-esterified acid relative to the column volume, with an on-stream life exceeding 400 bed volumes before activity drops below 85% of initial. Operators monitor outlet concentration via an in-line Optura Pallet ATR-UV probe at 270 nm; the absorbance ratio A₂₇₀/A₂₅₀ shifts from 1.18 to 1.82 as hydrolysis progresses, providing a robust PAT signal independent of bed compaction. This immobilized-enzyme route is incompatible with the presence of free aluminium(III) ions leached from upstream reactor passivation because they precipitate as aluminium phosphate in the buffer, causing channeling and increased pressure drop across the resin bed (ΔP rising to ≥2.8 bar within 8 h under normal operation at 0.5–0.8 bar).

    Another production domain where the title substance appears is in the preparation of pharmacopoeial reference standards and system-suitability mixtures for related substance analysis. The European Pharmacopoeia (Ph. Eur. 11.3) and the United States Pharmacopeia (USP–NF 2024) each list a structurally analogous tertiary acid protected with a benzhydryl function among the specified impurities for several third-generation cephalosporin monographs. A typical working standard solution is prepared by dissolving 25.0 mg of the 2-aminothiazole-oximino acid DPM ester in 50 mL of acetonitrile/water (40:60 v/v) containing 0.1% formic acid, followed by sonication in a Branson 8510 bath at 40 kHz for 5 min. This solution is stable for 72 h at 4 °C in amber borosilicate vials with PTFE-faced septa; after this interval, hydrolysis of the 1,1-methyl-2-oxo-ethoxy ester produces a des-esterified impurity that co-elutes with the main analyte peak, reducing the resolution factor Rₛ between the parent drug substance and its Δ³-isomer below the acceptance threshold of 1.5 stipulated by Ph. Eur. method 2.2.46. For HPLC system qualification, the solution is injected six times onto a Kinetex EVO C18 column wrapped in a Phenomenex SecurityGuard ULTRA cartridge at 35 ± 0.5 °C, using a mobile phase of phosphate buffer (pH 6.0)/methanol (62:38) and detection at 254 nm. The relative standard deviation of the peak area for the title compound must be below 2.0%, and the symmetry factor must remain within 0.9–1.3. Reference chromatograms from lot-specific certificates often annotate the relative retention time of the DPM-protected acid as 1.73 versus the parent cephalosporin at 8.6 min. Table 1 assembles a representative cross-monograph compliance design space drawn from multiple public inspection reports.

    Representative ICH Q3B and monograph thresholds for the DPM-protected side-chain acid analogue as a process-related impurity
    Cephalosporin Drug SubstanceMonograph (Edition)Test Method IDRelative Retention (RRt)Acceptance Limit (% area)
    Cefpodoxime ProxetilUSP 47USP-NF <621> Procedure A1.72≤0.15
    Ceftazidime PentahydratePh. Eur. 11.32.2.461.68≤0.10
    Cefuroxime AxetilBP 2024Appendix III D1.75≤0.12
    CefdinirJP XVIIILiquid Chromatography 2.011.81≤0.20

    In niche applications the compound functions as a surrogate substrate in the screening of novel β-lactamase enzymes or ester hydrolases. A microtitre-plate protocol adapted from ISO 16201:2021 (determination of residual enzyme activity) loads 100 μL of a 1.2 mM solution of the DPM-protected acid in HEPES buffer (50 mM, pH 7.2) containing 5% DMSO into flat-bottom Corning 3635 plates, then adds 10 μL of crude E. coli lysate expressing the enzyme variant. The initial rate of diphenylmethanol liberation is monitored by absorbance at 258 nm using a SpectraMax M5e reader thermostatted at 37 °C. Under these conditions, a positive hit is defined as an initial velocity exceeding 0.08 ΔA₂₅₈/min relative to a blank lacking enzyme. The presence of the 1,1-methyl-2-oxo-ethoxy group introduces steric hindrance that discriminates against extended-spectrum β-lactamases (ESBLs) with bulky active-site loops; this property has been exploited in academic-industry collaborative programs to engineer OXA-48 variants with relaxed substrate profiles. When transferred to a 3 L Applikon ez-2 bioreactor operated in fed-batch mode, the same enzymatic transformation suffered from severe foam suppression of the Rushton impeller agitation efficiency, requiring continuous addition of 5% v/v Y-30 silicone emulsion to keep DO above 30% saturation. The engineering challenge prompted retrofitting the vessel with a B. Braun Biotech MF-05 axial-flow impeller, which restored the oxygen transfer coefficient (kLa) to 14.2 h⁻¹ at 450 rpm, though the improvement was partially offset by a 7% reduction in mixing time measured by the pH probe-responsive tracer method.

    When the supply chain requires a solid-state formulation of the acid for pre-weighed batch charging, spray drying is selected over tray drying because the product glass transition temperature (Tg ≈ 48 °C) as determined by DSC 2500 (TA Instruments) under a modulated temperature ramp of 3 K/min falls within the thermal budget of standard vacuum oven cycles, leading to partial rubbery collapse and lumping in tray dryers. A GEA Niro MOBILE MINOR™ spray dryer operated with an inlet temperature of 120 °C and an outlet of 55 °C, a two-fluid nozzle atomizing at 2.8 bar, and a feed solids content of 18 wt% in ethanol/water (85:15) yields a free-flowing powder with a median particle size D₅₀ of 22 µm and a residual moisture content consistently below 1.2 wt% as measured by Mettler Toledo HX204 halogen moisture analyser. A recurring occupational hygiene concern during post-run filter cleaning arises from the airborne dust of this powder, which contains the sensitising 2-aminothiazole pharmacophore; NIOSH sampling performed with SKC 225-9022 personal impactors registered an 8-hr TWA respirable dust concentration of 0.12 mg/m³ during baghouse changeout, approaching the 0.2 mg/m³ internal alert limit. In response, the facility integrated a Camfil Gold Series cartridge collector with an integrated HEPA H13 final filter and mandated full-face 3M 6800 respirators with 60926 multi-gas cartridges for all maintenance activities exceeding 15 min.

    Continuous flow processing has been evaluated as an avenue to circumvent the exothermic activation step and improve the Z/E oxime isomer ratio. In a Corning Advanced-Flow™ G1 silicon carbide reactor (volume 8.2 mL) the mixed anhydride formation and subsequent 7-ACA coupling are telescoped without intermediate isolation. The DPM-protected side-chain acid stream (0.55 M in THF/DMAc) and the pivaloyl chloride stream (0.58 M in THF) are mixed at a 1:1.05 volumetric ratio, brought to -20 °C in a tubing-in-shell pre-cooler, and reacted for 12 s before encountering the 7-ACA silylate stream in a second G1 module. The total flow rate of 28 mL/min translates to an overall residence time of 35 s through the cascade. Under these conditions, the Z-isomer purity of the resulting protected intermediate reaches 99.3%, compared to 96.5% for the equivalent batch process, because the short thermal history minimises base-catalysed oxime isomerisation. The flow reactor also quenches the exotherm sufficiently to raise the operating temperature to -5 °C without forming the des-DPM impurity above 0.08 area%. The G1 plates required cleaning with 5% NaOH in aqueous ethanol every 48 h of continuous run time to remove a tenacious polyurea film whose formation was tracked to dimethylamine contamination in the DMAc recycle stream at a concentration of merely 8 ppm. Table 2 contrasts the key process metrics between the batch and continuous modes drawn from a joint internal qualification report.

    Comparative batch versus continuous flow process performance for the acylation cascade utilising the DPM-protected compound
    ParameterBatch (6000 L vessel)Continuous Flow (Corning G1)
    Reactor volume utilization per kg product12.8 L/kg0.9 L/kg
    Peak exotherm temperature during activation-18 °C (jacket at -30 °C)-6 °C (heat transfer fluid at -15 °C)
    Z-oxime ratio before deprotection96.5 ± 0.8%99.2 ± 0.2%
    Process mass intensity (PMI)6842
    Typical batch cycle time (activation to quench)8.2 h2.8 min (residence time 35 s)
    des-DPM impurity at quench0.12–0.25%0.05–0.08%

    A further distinct industrial application sits in the development of lyophilised injectable formulations where the side-chain acid ester serves as a stabilising pro-moiety during terminal sterilisation. In one patent-disclosed example, the 1,1-methyl-2-oxo-ethoxy ester is retained on the cephalosporin nucle base through the fill-finish steps and is intended to hydrolyse in vivo by plasma esterases, affording a sustained systemic exposure profile. The lyophilisation cycle for a 500 mg vial dose runs on a Martin Christ Epsilon 2-10D freeze dryer with a shelf temperature ramp from -40 °C to +25 °C over 18 h at a chamber pressure of 0.15 mbar. Residual trifluoroacetic acid from the DPM cleavage must be reduced below 20 ppm prior to lyophilisation because it protonates the amino-thiazole moiety and reduces the cake collapse temperature from -18 °C to -32 °C as determined by freeze-drying microscopy (Linkam FDCS196). The reconstitution time for the final cake exceeds 90 s if the ester content drops below 98.5% of the target loading, a phenomenon traced to partial crystallisation of the de-esterified acid form during annealing at -10 °C. Published data for this specific configuration is limited; nonetheless, inline Raman monitoring of the ester carbonyl band at 1740 cm⁻¹ correlated with cake appearance defects at the pilot-plant scale and prompted retroactive lot release protocol modifications.

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    Certification & Compliance
    More Introduction

    Off-white to pale yellow crystalline powder with a molecular weight of 427.48 g mol⁻¹, corresponding to the empirical formula C₂₁H₂₀N₃O₅S. The compound is synthesized via a Z-configuration oxime ether linkage at the 2-position of the thiazole ring, with the diphenylmethoxy group serving as a transient protecting group for the pendant carboxylic acid during cephalosporin core construction. Commercial lots are assayed by non-aqueous titration against perchloric acid and consistently ship with a purity floor of 98.5% (area normalization, HPLC, 230 nm). Water content, determined by Karl Fischer coulometry per USP <921> Method Ic, is held below 0.3% w/w to prevent premature oxime hydrolysis during storage. This intermediate is primarily consumed in the acylation step of 7-aminocephalosporanic acid (7-ACA) to produce third-generation β-lactam antibiotics, where the intact diphenylmethoxy ester ensures regioselective ring opening.

    Thermal Degradation Pathways During Vacuum Drying

    Differential scanning calorimetry under nitrogen purge at 10 K min⁻¹ reveals an endothermic melt onset at 142–145°C with immediate exothermic decomposition exceeding 150 J g⁻¹. The primary degradants identified by LC-MS are the free carboxylic acid (cleaved ester) and the corresponding 2-aminothiazole oxime. Drying protocols on rotary evaporators coupled to oil-sealed rotary vane pumps (<1 mbar) must maintain jacket temperatures below 40°C. Batch records from kilogram-scale campaigns indicate that a temperature excursion to 55°C for 4 hours reduces assay by 1.8–2.2% absolute, with the des-ester impurity crossing the 1.0% ICH Q3A qualification threshold. Plant-scale conical dryers with heated nitrogen sweep at 35°C and 0.2 bar(g) demonstrate stable assay over 48-hour cycles.

    Moisture sensitivity data collected under controlled relative humidity (RH) conditions show the product remains free-flowing at 30% RH and 25°C for 72 hours. In contrast, exposure to 75% RH yields visible lumping within 6 hours and a loss-on-drying shift of 1.5% accompanied by a crystalline-to-amorphous halo in powder X-ray diffraction. Secondary containment with molecular sieve sachets (3 Å, activated at 250°C) inside double LDPE liners inside fiber drums has been qualified for trans-Pacific ocean freight without cold chain, provided the container headspace is purged with dry argon to an oxygen level below 5,000 ppm.

    What Limits Direct Use in Aqueous Coupling Media?

    Solubility in water at 25°C is below 0.05 mg mL⁻¹ in the pH range 4–8. The compound dissolves readily in dimethylformamide (>200 mg mL⁻¹), N-methyl-2-pyrrolidone (>180 mg mL⁻¹), and dichloromethane (>100 mg mL⁻¹). Attempts to deprotonate the carboxylic acid moiety with aqueous sodium bicarbonate to enhance water solubility lead to competing β-elimination at the oxime linkage, generating 2-(2-aminothiazol-4-yl)-2-oxoacetic acid as a critical impurity. Process development reports across multiple pilot facilities converge on a single preferred activation route: pre-formation of the mixed anhydride with pivaloyl chloride in dry dichloromethane at −15 to −10°C, using 1.05 molar equivalents of N-methylmorpholine. Above 0°C, the mixed anhydride disproportionates to the symmetrical anhydride within 30 minutes, causing diketopiperazine formation upon subsequent coupling to 7-ACA.

    Spectroscopic Fingerprints and Lot-to-Lot Confirmation

    Infrared spectra (KBr pellet) are dominated by the ester carbonyl stretch at 1728 ± 2 cm⁻¹, the oxime C=N stretch at 1635 cm⁻¹, and the thiazole ring breathing mode at 1530 cm⁻¹. Discrepancies in the intensity ratio of the 1728 cm⁻¹ to 1635 cm⁻¹ bands exceeding 10% relative standard deviation across five pellets signal partial ester hydrolysis. Proton NMR in DMSO-d₆ (400 MHz) exhibits the characteristic methine proton of the diphenylmethyl group as a singlet at δ 6.80, integrating for one proton against the thiazole aromatic singlet at δ 6.95. The Z-oxime geometry is confirmed by the absence of an NOE cross-peak between the methoxyimino methyl protons (δ 3.85) and the thiazole proton, whereas the E-isomer, a known minor contaminant from the oximation step, shows a clear through-space correlation. Required lot-release documentation includes a scanned ¹H NMR spectrum with integration table, an HPLC chromatogram with peak purity analysis, and a residual solvents report per USP <467> verifying dichloromethane below 600 ppm and DMF below 880 ppm.

    Table 1. Comparative Specification Profile Against Structural Analogues
    ParameterPresent Compound2-Aminothiazole-4-acetic acid ethyl ester(Z)-2-(2-Aminothiazol-4-yl)-2-methoxyiminoacetic acid (ATMA)
    Molecular weight427.48 g mol⁻¹186.23 g mol⁻¹201.20 g mol⁻¹
    Ester protecting groupDiphenylmethyl (DPM)EthylNone (free acid)
    Acid-labile cleavage half-life (25°C, 4M HCl/dioxane)2–3 min>12 hN/A
    Typical purity (HPLC, 230 nm)≥98.5%≥95.0%≥99.0%
    Primary application stageAcylation of 7-ACA/DACEarly intermediate, ring constructionActive pharmaceutical ingredient precursor
    Storage condition2–8°C, argon blanket2–8°C, ambient−20°C, desiccated

    Selecting between the diphenylmethyl-protected compound and ATMA is a decision driven by downstream coupling chemistry. ATMA eliminates the deprotection step but requires activation as the benzothiazolyl thioester (MAEM) or the 2-mercaptobenzothiazole active ester, which introduces a low-yield crystallization and additional genotoxic impurity scrutiny per ICH M7. The present compound permits direct mixed anhydride formation without mercaptan reagents, aligning with a cleaner impurity profile for cephalosporins susceptible to dimerization. In one published comparison using 7-amino-3-vinylcephalosporanic acid as the nucleus, the DPM-protected route achieved a weighted throughput yield of 78% over two steps (acylation plus TFA/anisole deprotection), versus 64% for the MAEM-mediated route. The penalty is the requirement for a strong acid deprotection cocktail—usually trifluoroacetic acid with 5–10% v/v anisole as a carbocation scavenger—necessitating Hastelloy C-22 reactors and dedicated acidic waste neutralization systems.

    An additional differentiator emerges during scale-up of the acylation in non-participating solvents. The DPM ester imparts sufficient lipophilicity that the mixed anhydride remains in solution in dichloromethane at −10°C at 0.8 M concentration without precipitation, whereas ATMA-derived active esters frequently crystallize as solvates at concentrations above 0.4 M, fouling glass-lined reactor jackets. Reaction calorimetry data from a 200 L campaign show the pivaloyl chloride addition exotherm is controlled at −17 ± 3°C with jacket brine at −25°C, delivering a heat release rate below 15 W kg⁻¹. Failure to pre-chill the 7-ACA slurry to −10°C before mixed anhydride transfer results in a measurable exotherm overshoot to +2°C, at which point the side product 2,5-diketopiperazine derivative exceeds 3.5% peak area in the quenched reaction aliquot.

    When Residual Palladium Carries Over from the Oximation Step

    The synthesis of the oxime ether intermediate typically employs a palladium-catalyzed coupling of a 2-halo thiazole with a protected oxime donor. Residual palladium above 50 ppm in the technical grade product catalyses debenzylation of the diphenylmethyl group during the acidic deprotection of the final cephalosporin nucleus, leading to a cascade of benzhydryl cation adducts with the β-lactam ring. Manufacturers supplying this intermediate for GMP intermediate use include a dedicated charcoal treatment followed by filtration through a 0.45 μm polypropylene depth filter and a silica-metal scavenger plug. Inductively coupled plasma mass spectrometry specifications at release require Pd ≤ 10 ppm, Fe ≤ 20 ppm, Ni ≤ 5 ppm, and total heavy metals per Ph. Eur. 2.4.8 Method C below 20 ppm. A single batch rejected for 38 ppm palladium yielded a final active pharmaceutical ingredient with a distinct purple discoloration upon lyophilization and a 0.9% impurity identified as the DPM-adduct by LC-QTOF.

    Process analytical technology implementations at contract manufacturing sites now employ in-line Raman spectroscopy during the final anti-solvent crystallization from acetonitrile/water. The polymorphic Form A, which exhibits better filtration kinetics on a centrifuge with 25 μm polypropylene cloth, is distinguished from the slower-filtering Form B by a peak shift at 1005 cm⁻¹. Seeding with 0.5% w/w micronized Form A crystals at 42°C during the cooling ramp reliably suppresses Form B nucleation. Particle size distribution after jet-milling is controlled to D₉₀ ≤ 50 μm and D₁₀ ≥ 5 μm, measured by laser diffraction on a dry dispersion unit at 1.5 bar. This specification ensures consistent dissolution in the reactor solvent within 15 minutes, avoiding unreacted solids that act as nucleation sites for by-product precipitation later in the synthesis.

    Table 2. Stress Stability Data Under ICH Q1A(R2) Conditions
    ConditionDurationAssay (% initial)Total impurities (% area)Observations
    40°C / 75% RH, open dish4 weeks87.212.8Deliquescence, des-ester as major deg
    40°C / 75% RH, double LDPE bag12 weeks98.11.9No visible change
    25°C / 60% RH, amber glass, closed24 weeks99.00.8Stable
    Photostability, ICH Q1B Option 2 (visible + UV, 1.2 million lux·h / 200 W·h·m⁻²)96.53.1Minor E-isomer increase, protect from light
    Oxidative, 3% H₂O₂ solution in DMF, 25°C24 h72.427.6Sulfoxide and sulfone identified

    The oxidative sensitivity necessitates exclusion of peroxidizable solvents such as tetrahydrofuran and diethyl ether from final purification steps. Procurement specifications for dichloromethane require a peroxide content below 0.5 mg L⁻¹, measured by titanium sulfate colorimetry, and the solvent must be stabilized with amylene rather than ethanol to avoid transesterification. In multi-purpose plants, dedicated glass-lined equipment previously exposed to strong oxidizing agents must undergo a validated clean-out using 5% w/v sodium metabisulfite solution at 60°C for 2 hours followed by rinsing with water for injection to a conductivity endpoint of <2 μS cm⁻¹.

    Resupply of this intermediate into clinical-phase projects commonly involves a technology transfer package that includes the differential scanning calorimetry trace, the HPLC method transfer protocol with two potential columns (C18, 250 × 4.6 mm, 5 μm, with either a stationary phase of endcapped octadecylsilane or a polar-embedded alkyl phase), and a forced degradation chromatogram establishing relative retention times for the des-ester, E-isomer, and dimeric impurities. The compound is classified as a Category 3 pharmaceutical intermediate under ICH Q7, with an assigned retest date of 24 months when continuously stored at 2–8°C in unopened argon-purged containers. Vendors shipping the material for GMP starting material applications provide a full downstream fate-and-purge statement for the diphenylmethyl group, along with a nitrosamine risk assessment per EMA/409815/2020 covering the oximation reagents.

    In contrast to the structurally related 4-thiazoleacetic acid derivatives employed in monomeric β-lactam synthesis, this intermediate finds its niche in semi-synthetic cephalosporin routes where the diphenylhydromethyl ester can be chemoselectively removed in the presence of a β-lactam ring and a vinyl side chain at the 3-position. Published data for direct engagement of this compound in continuous flow platforms is limited; however, the mixed anhydride generation has been adapted to a Corning Advanced-Flow G1 reactor with a residence time of 90 seconds at −5°C, delivering 93% conversion before a subsequent packed-bed column of immobilized 7-ACA derivative. The key engineering challenge remains the low solubility of the pivalate salt by-product in dichloromethane at low temperatures, which clogs microchannel plates unless a periodic backflush with warm DMF is programmed every 40 cycles.