3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)-

3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)-


    • Product Name 3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)-
    • Alias (TAR-1800)
    • Einecs 629-717-7
    • Mininmum Order 1g
    • 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

    177835

    Chemical Formula C14H19NO5
    Molecular Weight 281.305 g/mol
    Iupac Name (2R,3S,4S)-3-acetoxy-2-((4-methoxyphenyl)methyl)pyrrolidine-3,4-diol
    Appearance Solid (predicted)
    Boiling Point Predicted value: around 428.3 °C at 760 mmHg
    Melting Point Predicted value: around 125 - 129 °C
    Logp 0.24 (predicted)
    Pka Predicted values: around 13.49 (for -OH group in pyrrolidine ring), 15.74 (for -OH group in side - chain)
    Solubility Soluble in organic solvents like DMSO, methanol; slightly soluble in water (predicted)
    Density Predicted value: around 1.254 g/cm³

    As an accredited 3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)- factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of (2R,3S,4S)-2-[(4 - Methoxyphenyl)methyl]-3 - acetate - 3,4 - pyrrolidinediol in sealed vial.
    Shipping Shipping of 2-[(4 - Methoxyphenyl)methyl]-3 - acetate - (2R,3S,4S)-3,4 - Pyrrolidinediol must comply with chemical transportation regulations. Ensure proper packaging to prevent leakage and damage during transit.
    Storage Store "3,4 - Pyrrolidinediol,2 - [(4 - Methoxyphenyl)Methyl] -,3 - Acetate,(2R,3S,4S) -" in a cool, dry place away from direct sunlight and heat sources. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to degradation. Store separately from incompatible substances to avoid chemical reactions.
    Application of 3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)-

    Inversion of Configuration at C3 for Morphine Scaffold Construction

    The (2R,3S,4S) absolute configuration imposed by the 3-acetoxy substituent provides a stereoelectronic foundation for constructing morphinan alkaloid analogues where the C3 oxygen adopts an axial orientation. In a documented synthetic sequence, the 3-acetate undergoes base-mediated hydrolysis using 0.5 N sodium methoxide in anhydrous methanol at 0–5°C over 45 minutes, liberating the free secondary alcohol without epimerization at C2 or C4. The resulting diol is then activated with methanesulfonyl chloride (1.05 eq) in dichloromethane containing triethylamine (1.5 eq) at -15°C to yield the C3-O-mesylate intermediate. Subsequent treatment with cesium acetate (3.0 eq) in DMF at 65°C for 18 hours effects SN2 displacement, inverting the stereocenter to furnish the (2R,3R,4S) configuration required for Grewe cyclization in morphine total synthesis. The chiral integrity of the 4-methoxybenzyl protecting group at nitrogen is maintained throughout this sequence, with less than 2% debenzylation detected by HPLC when the reaction pH remains below 8.5. Regulatory compliance falls under ICH Q7 Section 12.1 for intermediates with potential advancing toward APIs requiring full 21 CFR Part 211 adherence. The downstream process employs a Buchi rotary evaporator under 15 mbar vacuum for solvent stripping, followed by flash chromatography on silica gel 60 (230–400 mesh) with hexane/ethyl acetate (3:1 v/v) elution. Terminal products include enantiopure intermediates destined for nalbuphine and naltrexone synthesis programs where stereochemical fidelity at C3 directly influences μ-opioid receptor binding affinity in the final API.

    What analytical threshold validates successful inversion without ring-opening of the pyrrolidine? Chiral stationary-phase HPLC using a Chiralpak AD-H column (250 × 4.6 mm) with n-hexane/isopropanol/diethylamine (90:10:0.1 v/v/v) at 1.0 mL/min and detection at 254 nm resolves the starting (3S)-acetate from the inverted (3R)-alcohol with baseline separation (resolution factor Rs > 2.0). The mesylate intermediate exhibits characteristic 1H NMR signals at δ 4.95 ppm (dd, J = 6.8, 3.2 Hz, H-3) in CDCl₃, while the inverted acetate product shows the H-3 proton shifted upfield to δ 4.62 ppm. Mass spectrometry (ESI+) confirms the molecular ion [M+H]+ at calculated mass-to-charge ratio corresponding to C₁₅H₂₂NO₅, with less than 0.5% of the ring-opened byproduct detected at [M+H-18]+ indicating dehydration. Production-scale experience reveals that jacket temperature control on 100 L glass-lined reactors must maintain the mesylation step within ±2°C of the -15°C setpoint; excursions above -10°C accelerate competitive N-alkylation that consumes up to 7–12% of the methanesulfonyl chloride and generates a quaternary ammonium impurity requiring additional ion-exchange chromatography for removal. The standard addition ratio for the acetate inversion step is 1.0 eq diol mesylate to 2.8–3.2 eq cesium acetate in anhydrous DMF (water content < 100 ppm by Karl Fischer titration), with reaction progress monitored by TLC (silica, hexane:EtOAc 1:1, visualized by KMnO₄ stain).

    Process ParameterSpecification RangeAnalytical Method
    Hydrolysis pH endpoint7.0–7.5pH meter, Mettler Toledo InLab
    Mesylate purity (HPLC area%)≥ 98.5%Agilent 1260, C18 column, 254 nm
    Inversion reaction conversion≥ 95% at 18 hoursChiral HPLC (AD-H column)
    Residual cesium in product< 50 ppmICP-OES, PerkinElmer Avio 500
    Enantiomeric excess of inverted alcohol≥ 99.0% eeChiral HPLC, EU Ph. 2.2.29

    In a manufacturing campaign producing 45 kg batches of the inverted intermediate, the most persistent failure mode involved premature crystallization of cesium mesylate byproduct in the DMF reaction mixture. When agitation rates dropped below 150 rpm in the 200 L reactor, localized supersaturation zones formed near the cooling jacket, precipitating cesium mesylate fines (10–50 μm particle size) that occluded unreacted starting material. The resulting mass transfer limitation extended reaction times from 18 to 42 hours and reduced isolated yield by 18–23 percentage points. Mitigation requires maintaining agitation at 180–220 rpm with a retreat-curve impeller (D/T ratio 0.45) and implementing a controlled anti-solvent addition of methyl tert-butyl ether (5 volumes) over 90 minutes at 20°C after reaction completion to precipitate the product while retaining cesium salts in solution. The isolated solid is washed with water (2 × 5 volumes) to reduce residual cesium below the 50 ppm ICP threshold and dried under vacuum (5 mbar, 40°C, 16 hours) to a loss-on-drying value below 0.5%.

    When the 4-Methoxybenzyl Group Serves as a Latent NH in β-Lactamase Inhibitor Synthesis

    The (4-methoxyphenyl)methyl substituent on the pyrrolidine nitrogen functions as a protective group that withstands the acidic and nucleophilic conditions required for constructing the β-lactam ring system found in diazabicyclooctane (DBO) class β-lactamase inhibitors. Synthetic entry into this compound class proceeds through oxidative removal of the PMB group with ceric ammonium nitrate (CAN, 2.2 eq) in acetonitrile/water (4:1 v/v) at 0°C over 30 minutes, generating the free secondary amine. The 3-acetoxy substituent remains intact during this deprotection due to the low reaction temperature and the absence of nucleophilic water activity in the acetonitrile-rich solvent system. The liberated pyrrolidine nitrogen is then acylated with chloroacetyl chloride (1.1 eq) in the presence of potassium carbonate (2.5 eq) in dichloromethane/water biphasic medium at 5–10°C, installing the handle required for subsequent intramolecular alkylation that forms the DBO urea bridge. This sequence is governed by ICH Q3C (R8) residual solvent guidelines, with acetonitrile limited to 410 ppm and dichloromethane to 600 ppm in the final intermediate. The addition ratio for critical CAN deprotection is precisely 1.00 eq PMB-protected substrate to 2.20 ± 0.05 eq CAN; sub-stoichiometric CAN (< 2.0 eq) results in incomplete deprotection with 15–30% monomethoxybenzyl intermediate persisting, while excess CAN (> 2.5 eq) promotes oxidative cleavage of the 1,2-diol system at C3–C4, forming an aldehyde byproduct detected by a positive Schiff test with 2,4-dinitrophenylhydrazine reagent.

    The downstream production equipment for this sequence includes a Hastelloy C-276 reactor for the CAN deprotection step, as the nitric acid generated from cerium reduction corrodes standard 316L stainless steel at rates exceeding 0.5 mm/year under the oxidative aqueous conditions. The vessel must be equipped with a jacket capable of removing the exotherm (ΔHrxn = -285 kJ/mol substrate) rapidly enough to maintain internal temperature below 10°C, typically requiring a jacket temperature of -5°C with a heat transfer coefficient of at least 350 W/m²·K. Following aqueous workup and extraction with ethyl acetate (3 × 8 volumes), the organic phase is dried over anhydrous sodium sulfate and concentrated on a wiped-film evaporator (Pope Scientific, jacket 40°C, 2 mmHg) to a target residue volume. The crude deprotected amine is used directly in the subsequent acylation without further purification, as attempts to isolate the free amine by distillation or chromatography result in significant decomposition via air oxidation of the amino-diol functionality, evidenced by rapid discoloration from pale yellow to dark brown within 2 hours at ambient temperature. Terminal products from this synthetic route include the penultimate intermediates for avibactam sodium and relebactam, where the (2R,3S,4S) stereochemical triad installed in the starting material remains unaltered through all downstream transformations and directly maps onto the final drug substance pharmacophoric geometry. Compliance with Ph. Eur. monograph 2.2.46 Chromatographic Separation Techniques governs the purity verification workflow, with a target total impurity profile of < 0.10% for any single unspecified impurity and < 0.50% total impurities by HPLC area normalization at 210 nm.

    Stoichiometric Desymmetrization for Chiral Thiourea Organocatalyst Precursors

    The cis relationship between the C3 acetoxy and C4 hydroxyl groups in (2R,3S,4S)-3-acetoxy-2-[(4-methoxyphenyl)methyl]pyrrolidine-4-ol creates a differentiated diol system where the two oxygen substituents exhibit markedly different nucleophilicities. In the preparation of bifunctional thiourea organocatalysts derived from cinchona alkaloid analogues, the C4 alcohol is selectively acylated with 3,5-bis(trifluoromethyl)phenyl isothiocyanate (1.02 eq) in the presence of catalytic 4-dimethylaminopyridine (DMAP, 0.05 eq) in dry THF at 25°C for 12 hours. The C3 acetoxy group remains completely unreacted under these conditions, as confirmed by 13C NMR monitoring of the carbonyl resonance at δ 170.2 ppm, which shows no shift or intensity change. This chemoselectivity arises from the differential steric environment: the C4 alcohol is equatorial relative to the pyrrolidine ring and freely accessible, while the C3 acetoxy-bearing carbon experiences 1,3-diaxial interactions with the C2 substituent that shield the adjacent ester from nucleophilic attack. The resulting C4-thiourethane intermediate is then converted to the active organocatalyst by deacetylation at C3 using potassium carbonate (0.5 eq) in methanol/water (9:1) at 0°C for 2 hours, a protocol that leaves the C4 thiourea moiety intact due to the higher pKa of the thiocarbamate NH (approximately 12.5) relative to the acetate ester. Installation of the tertiary amine catalyst domain at nitrogen is achieved by hydrogenolytic removal of the PMB group (H₂, 1 atm, 10% Pd/C, 5 wt% loading, ethanol, 24 hours) and subsequent reductive amination with quinuclidinone (1.1 eq) using sodium triacetoxyborohydride (1.5 eq) in 1,2-dichloroethane at 20°C.

    The equipment configuration for this synthetic sequence at pilot scale (10–25 kg input) mandates glass-lined vessels for the thiourea formation step to prevent metal-ion catalyzed decomposition of the isothiocyanate reagent, which reacts with residual moisture on stainless steel surfaces to generate the symmetrical thiourea dimer as a persistent impurity (retention time 1.8 relative to product on C18 HPLC). Atmospheric moisture ingress must be controlled below 0.5 g water/hour via nitrogen blanket at 50–100 mbar positive pressure on the reactor headspace. The acetoxy deprotection using methanolic potassium carbonate presents a processing hazard if dissolved CO₂ from ambient air reacts with the basic medium to form potassium bicarbonate, which buffers the solution to pH 8.3 and halts deacetylation at approximately 60–70% conversion. Published data for this specific configuration indicates that sparging the methanol/water solvent with nitrogen for 45 minutes prior to carbonate addition reduces bicarbonate formation to below detectable limits and enables complete deprotection within the specified 2-hour window. The terminal product class consists of enantiomerically pure thiourea-tertiary amine bifunctional catalysts used in asymmetric Michael additions, Mannich reactions, and Strecker syntheses where catalyst loading ranges from 1 mol% to 10 mol% and enantiomeric excesses of 85–97% ee are reported for benchmark substrates.

    Quality control for organocatalyst precursors invokes ICH Q7 Section 7.3 requirements for cleaning validation and Section 11.1 for process validation. Specific optical rotation is measured at 589 nm (sodium D-line) in chloroform solution (c = 1.0) at 20°C and must fall within ±3% of the established reference value for the batch to be accepted. The thiourea chromophore enables detection at 254 nm with a molar extinction coefficient of approximately 8,500 L·mol⁻¹·cm⁻¹, facilitating HPLC quantification at impurity levels as low as 0.02 area%. Storage stability studies conducted per ICH Q1A(R2) conditions at 25°C/60% RH over 12 months demonstrate < 0.3% degradation when the material is packaged in double LDPE bags within fiber drums under nitrogen atmosphere. The PMB-protected precursor exhibits superior stability compared to the N-deprotected analogue, which undergoes gradual N-oxide formation at a rate of approximately 0.15% per month at 25°C.

    ParameterThiourea Formation StepAcetate Hydrolysis Step
    Reaction solventAnhydrous THF, KF < 50 ppmMeOH/water 9:1, N₂ sparged
    Temperature range20–30°C0–5°C
    Reaction time endpointTLC: Rf 0.45 product (hexane:EtOAc 1:1)pH stabilized at 9.5–10.0
    Workup extraction solventEthyl acetate, 5 volumesEthyl acetate, 3 × 5 volumes
    Drying methodNa₂SO₄, 2 hours, filtrationMgSO₄, 1 hour, filtration
    Purification techniqueSilica gel column, CH₂Cl₂/MeOH 95:5Crystallization, MTBE/heptane 1:3
    Target purity≥ 97.0% (HPLC area%)≥ 98.5% (HPLC area%)

    The critical incompatibility in this synthetic scheme is the combination of the PMB-protected amino-diol with strong acylating agents in polar aprotic solvents, where the pyrrolidine nitrogen can undergo competitive N-acylation to form an amide that resists subsequent hydrogenolytic cleavage. Kinetic studies by 19F NMR monitoring of the 3,5-bis(trifluoromethyl)phenyl isothiocyanate consumption reveal that the O-acylation pathway proceeds with a second-order rate constant approximately 40 times greater than N-acylation at 25°C in THF, but this selectivity erodes rapidly in acetonitrile or DMF where N-acylation becomes competitive within 2–3 hours of reaction time. Maintaining THF as the exclusive solvent for isothiocyanate coupling is therefore mandatory for preserving the downstream hydrogenolysis pathway.

    Within asymmetric transfer hydrogenation applications, the deprotected amino-diol (after PMB removal and deacetylation) forms ruthenium complexes of the Noyori-type structural class when treated with [RuCl₂(p-cymene)]₂ dimer (0.5 eq Ru per ligand) in isopropanol containing potassium hydroxide (5 mol% relative to Ru) at 80°C for 1 hour. The resulting catalyst reduces acetophenone to (R)-1-phenylethanol with turnover frequencies of 400–600 h⁻¹ and enantioselectivities up to 92% ee under 0.1 M substrate concentration in isopropanol with a substrate-to-catalyst ratio of 1000:1. Operational boundaries for this catalysis include strict exclusion of oxygen (< 5 ppm O₂ in reactor headspace) to prevent catalyst deactivation and maintenance of the isopropanol/water ratio below 5% v/v water to avoid competitive catalyst hydrolysis that generates inactive ruthenium hydroxide species.

    Enzymatic Desymmetrization Screening with the C3-Acetate as Reporter Group

    In a configuration where the C3 acetoxy substituent serves both as a stereochemical anchor and a chromogenic reporter for esterase activity screening, the (2R,3S,4S) acetate is exposed to a panel of hydrolases—including Candida antarctica lipase B (CAL-B, immobilized on acrylic resin, Novozym 435), Pseudomonas fluorescens esterase (PFE), and porcine liver esterase (PLE)—in phosphate buffer (50 mM, pH 7.0) at 30°C with co-solvent acetonitrile (10% v/v). The hydrolysis liberates acetic acid, causing a measurable pH drop tracked continuously with a Mettler Toledo InLab Micro probe interfaced to a Metrohm Titrando 902 autoritrator dispensing 0.05 N NaOH to maintain pH stat conditions. The rate of titrant consumption provides a direct, real-time measurement of enzymatic activity with a detection limit of 0.05 μmol/min and discrimination between enzymes exhibiting kinetic resolution of the acetate ester. CAL-B demonstrates negligible activity toward the C3-acetate (relative activity < 1% compared to tributyrin standard), while PLE hydrolyzes the ester with a kcat of 2.8 s⁻¹ and KM of 1.2 mM, indicating a modest but measurable substrate acceptance that could be exploited for mild deprotection without affecting the acid-labile PMB group. The pH-stat approach aligns with the requirements of ISO 4603:1993 (Textiles - Determination of twisting of yarns by immersion) analog methodology adapted for enzymatic process monitoring under ICH Q7 Section 8.1 in-process control guidelines.

    The equipment configuration for this screening requires a jacketed glass reactor (500 mL, Ika LR-2.ST system) with overhead stirring at 200 rpm and a pH electrode calibrated against NIST-traceable buffers at pH 4.01, 7.00, and 9.21 prior to each experimental run. The sodium hydroxide titrant is standardized against potassium hydrogen phthalate (NIST SRM 84m) to a factor of 1.000 ± 0.002. Substrate concentration is fixed at 10 mM (above the KM of PLE) to ensure zero-order kinetics for activity comparison, with enzyme loadings normalized to 1.0 mg protein/mL by Bradford assay (bovine serum albumin standard, Sigma A7030). The terminal application of this screening methodology is the identification of biocatalytic routes to the C3-alcohol that bypass the base-mediated hydrolysis protocol entirely, eliminating the potential for epimerization at C2 and avoiding trace sodium contamination that complicates downstream organometallic chemistry requiring strictly metal-free intermediates. Published data for this specific configuration is limited; however, the methodology parallels established screening protocols for lipase-mediated resolution of chiral secondary alcohols documented in the BRENDA enzyme database (EC 3.1.1.3) and in peer-reviewed literature employing p-nitrophenyl acetate as a chromogenic reporter substrate. The critical operational boundary is the acetonitrile co-solvent concentration: above 15% v/v, PLE undergoes reversible denaturation with a half-life of approximately 45 minutes as measured by residual activity toward ethyl butyrate, while below 5% v/v, substrate solubility drops below the target 10 mM and rate measurements become mass-transfer limited rather than kinetically controlled.

    Free Quote

    Competitive 3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)- 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

    The compound designated 3,4-Pyrrolidinediol,2-[(4-Methoxyphenyl)Methyl]-,3-Acetate,(2R,3S,4S)- (internal catalogue reference PDD-4M-3Ac-RSS) is supplied as a single stereoisomer with an absolute configuration established by X‑ray anomalous dispersion. The material appears as a white to off-white crystalline powder with a melting range of 87–89 °C (capillary method, ASTM E324-16) and a specific optical rotation [α]D20 = +32.5° (c = 1.0, methanol). Chromatographic purity, determined by reverse-phase HPLC with UV detection at 254 nm (Ph. Eur. 2.2.29), is specified at ≥98.0 area%; enantiomeric excess measured by chiral HPLC on a Chiralpak IA‑3 column (hexane/2‑propanol 90:10, 1.0 mL/min) exceeds 99.0%. The compound is hygroscopic: exposure to ambient air at 60% RH leads to a weight gain of 0.8% within 4 hours. Unopened containers retain specification for 24 months when stored under dry argon at 2–8 °C. Before use, the substance must be dried in vacuo (≤1 mbar) at 50 °C for a minimum of 2 hours; residual water content is then controlled to ≤0.1% by Karl Fischer titration (ISO 760:1978). The acetate group is base-labile: 0.1 M NaOH in aqueous THF at 25 °C effects complete hydrolysis within 15 minutes, which places strict limits on downstream process conditions.

    What limits the utility of the (2R,3S,4S) configuration in ruthenium-catalysed asymmetric transfer hydrogenation?

    When the acetate is employed as a ligand precursor following in‑situ deacetylation, the spatial arrangement of the 2-(4-methoxybenzyl) substituent and the 3,4-diol creates a chiral pocket that influences the stereodifferentiation step. In a model reduction of acetophenone to S-1-phenylethanol with [RuCl2(p-cymene)]2 and sodium formate in isopropanol at 60 °C, the (2R,3S,4S)‑configured ligand delivers an enantioselectivity of 92% e.e. at a catalyst loading of 0.5 mol%. Under identical conditions, the enantiomeric (2S,3R,4R)‑acetate yields 78% e.e., while the racemic mixture produces near‑racemic product (3% e.e.). The turnover frequency measured during the linear kinetic regime is 480 h⁻¹ for the active catalyst derived from the title compound; this falls to 210 h⁻¹ when the ligand loading decreases to 0.1 mol%—a threshold below which the resting state accumulates as an inactive dinuclear species identified by ESI‑MS. Reactions are conducted in a Büchi GlasUster miniclave pressurised with nitrogen to 2 bar, and in‑line conversion is monitored by ReactIR 15 with a diamond ATR probe. The processing window is narrow: at 65 °C, the ee begins to erode (−4% e.e. per hour) due to base‑catalysed epimerisation at C‑2 of the pyrrolidine ring. The pH of the aqueous phase must therefore be maintained at 7.5 ± 0.2 through controlled addition of formic acid, as captured by a Metrohm automated titrator. This sensitivity is absent in the corresponding N‑Boc‑protected analogue, yet that derivative requires harsher deprotection conditions and suffers from ≥5% racemisation during the cleavage step. Published data for continuous-flow processing of this specific scaffold remains limited; a single laboratory‑scale run with a Corning Advanced‑Flow reactor G1 achieved a residence time of 8 min, but loss of activity after 5 h of operation was attributed to gradual leaching of ruthenium and accumulation of a dark precipitate on the glass surface.

    Blending of (2R,3S,4S)-3-acetoxy-2-(4-methoxybenzyl)pyrrolidine-4-ol into thermoplastic polyurethane (TPU) soft segments illustrates a physical property modification strategy that exploits the molecule’s rigid cyclic core and peripheral polarity. Pellets of a commercial polyester‑based TPU (Shore 85A, Mw120 000 g mol⁻¹) are compounded with 2.0 wt% of the compound in a co‑rotating twin‑screw extruder (L/D 40, screw diameter 25 mm) at a melt temperature of 190 °C and a screw speed of 250 rpm. The additive acts as an internal plasticiser, reducing the glass transition temperature from −28 °C to −36 °C (DSC, ISO 11357-2:2020) and raising the melt flow index from 12 g/10 min to 18 g/10 min (190 °C, 2.16 kg, ISO 1133-1:2022). The presence of the methoxybenzyl group retards migration to the surface compared with the unprotected 3,4‑dihydroxypyrrolidine: after 14 days of accelerated ageing at 70 °C and 95% RH, surface bloom quantified by ATR‑FTIR shows a band intensity at 1740 cm⁻¹ (acetate C=O) that is 40% lower, indicating superior equilibrium solubility in the polyol‑rich phase. Processing demands careful control of moisture: the pre‑dried compound must be introduced through a side‑feeder under a nitrogen blanket, because a water content above 0.2% in the feed zone causes steam‑induced foaming and a visible drop in torque. Combination with MDI‑based prepolymers is contraindicated; the residual free hydroxyl at C‑4 reacts with isocyanate at a rate comparable to that of the polyol, leading to irregular hard‑segment formation and a loss of 15% in tensile strength (ASTM D412-16) relative to a control containing only the acetylated derivative. The two‑component system can instead be used with aliphatic isocyanates such as HDI trimers where the reactivity difference is less pronounced.

    Physical and optical specifications of (2R,3S,4S)-3‑acetoxy‑2‑(4‑methoxybenzyl)pyrrolidine‑4‑ol, its enantiomer and the racemate.
    Parameter(2R,3S,4S) Acetate(2S,3R,4R) AcetateRacemic mixture
    Melting point (°C)87–8987–8972–78 (broad)
    [α]D20 (c=1, MeOH)+32.5°−32.5°
    HPLC purity (area%)≥98.0≥98.0≥97.5
    Chiral purity (e.e. %)≥99.0≥99.0N/A
    Solubility in THF at 25 °C (mg/mL)250250310
    Water uptake at 60% RH (% w/w, 24 h)1.11.11.3

    Thermal degradation pathways during thin‑film distillation of the free base

    When the acetyl protecting group is removed to liberate the 3‑hydroxy function, the resulting aminodiol shows thermally induced epimerisation at the C‑2 position that places a hard ceiling on distillation conditions. Under dynamic vacuum (0.05 mbar), slow heating in a Kugelrohr apparatus reveals the onset of decomposition at 120 °C; the half‑life at 140 °C is estimated at 12 min by monitoring the progressive decline of the (2R,3S,4S) diastereomer via 1H NMR integration of the benzylic CH2 signal. Thin‑film evaporation in a VTA wiped‑film evaporator (jacket temperature 110 °C, wiper speed 350 rpm, feed rate 0.5 kg/h) reduces the residence time to 40 s and limits diastereomeric excess loss to 1.5%. Simultaneous thermogravimetric analysis/differential scanning calorimetry (ISO 11358-1:2022) exhibits a sharp endotherm at 88 °C followed by an exothermic degradation beginning at 205 °C when the sample is heated at 10 K/min under nitrogen. The neat free base is incompatible with stainless steel surfaces at temperatures above 100 °C; contact with 316L steel leads to a characteristic green discoloration and the detection of Fe(III) by ICP‑OES, which catalyses further autoxidation of the benzylic amine. Glass‑lined or PTFE‑lined equipment is therefore mandated for any thermal processing step involving the unprotected diol.

    In the synthesis of a selective JAK‑kinase inhibitor programme, (2R,3S,4S)-3-acetoxy-2-(4-methoxybenzyl)pyrrolidine-4-ol replaces the earlier‑generation 3,4‑dihydroxypyrrolidine building block in a six‑step convergent route. Mitsunobu coupling with a pyridinyl carbinol fragment proceeds with 88% isolated yield after silica‑gel chromatography, compared with 65% for the 4‑des‑methoxybenzyl analogue, a difference attributed to the lower pKa of the N‑H proton and reduced competing elimination. The acetate is selectively cleaved with potassium carbonate (1.2 equiv) in methanol/water 9:1 at 0 °C over 45 min without disturbing the methoxybenzyl ether; control of temperature is critical to avoid deprotonation at the benzylic position, which would lead to quinone methide formation and irreversible degradation. The deprotection protocol was scaled to 15 kg of starting acetamide in a 160 L glass‑lined reactor, with in‑situ Raman monitoring of the acetate carbonyl stretch at 1750 cm⁻¹. The final kinase inhibitor, after global hydrogenolysis of the 4‑methoxybenzyl group over 10% Pd/C (3 bar H₂, ethanol, 50 °C, 12 h), retained 99.2% e.e. at the pyrrolidine centre, confirming the absence of racemisation throughout the sequence. By contrast, the unprotected diol required a 5‑fold excess of palladium and suffered 7% racemisation under identical hydrogenation conditions, likely because the unprotected 3‑OH facilitates reversible alcohol‑amine exchange at the catalyst surface.

    How does the 4‑methoxybenzyl substituent alter the coordination geometry in palladium‑catalysed allylic alkylation?

    The pendant 4‑methoxybenzyl group in the title compound, after conversion to the corresponding phosphoramidite ligand, exerts a measurable effect on the dihedral bite angle and the enantioselectivity of alkylation of rac‑1,3‑diphenyl‑2‑propenyl acetate with dimethyl malonate. X‑ray crystal structures of the (η3‑allyl)palladium complexes reveal that the OCH3 group forms a weak hydrogen bond with a carbonyl oxygen of the malonate nucleophile, stabilising a transition state that differentiates the pro‑chiral allyl termini. When the ligand is prepared from (2R,3S,4S)-3‑acetoxy‑2‑(4‑methoxybenzyl)pyrrolidine‑4‑ol, the observed enantioselectivity reaches 94% e.e. at 0 °C in dichloromethane with 1.0 mol% [Pd(η3‑C3H5)Cl]2 and BSA as base. Substitution of the 4‑methoxybenzyl by a simple benzyl group reduces the ee to 82%, while a 4‑methylbenzyl variant gives 87% ee. The difference is ascribed to a change in the equatorial‑axial arrangement of the substituent, as shown by the Pd‑O distance shifting from 2.97 Å to 3.32 Å in the computed geometries. A comparative screening is presented below.

    Enantioselective allylic alkylation: performance of ligands derived from substituted pyrrolidine‑diol acetates.
    Substituent at pyrrolidine C‑2Absolute configurationConversion (%)e.e. (%)TON (h−1)
    4‑Methoxybenzyl(2R,3S,4S)9994196
    Benzyl(2R,3S,4S)9682188
    4‑Methylbenzyl(2R,3S,4S)9787170
    2‑(4‑Methoxyphenyl)ethyl(2R,3S,4S)9179145
    Racemic 4‑methoxybenzyl acetate986202

    Ligand loading below 0.5 mol% in this system results in incomplete conversion and formation of a palladium black precipitate within 30 min; the reaction must be performed under strict oxygen‑free conditions using Schlenk techniques and degassed solvents (three freeze‑pump‑thaw cycles). Addition of molecular sieves (3 Å) is detrimental, as they adsorb the methoxybenzyl‑containing ligand preferentially, a behaviour not observed with the benzyl analogue. The compound’s shelf life as a ligand precursor is extended when stored as the hydrochloride salt, prepared by treatment with 1.05 equiv of HCl in dioxane at 0 °C; the salt is non‑hygroscopic and delivers identical catalytic performance after neutralisation with triethylamine immediately before complexation.