1-{[(9H-Fluoren-9-Ylmethoxy)Carbonyl]Oxy}Pyrrolidine-2,5-Dione

1-{[(9H-Fluoren-9-Ylmethoxy)Carbonyl]Oxy}Pyrrolidine-2,5-Dione


    • Product Name 1-{[(9H-Fluoren-9-Ylmethoxy)Carbonyl]Oxy}Pyrrolidine-2,5-Dione
    • Alias Fmoc-ONSu
    • Einecs 402-790-1
    • Mininmum Order 1g
    • 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

    507600

    Chemical Formula C20H15NO5
    Molecular Weight 349.34 g/mol
    Appearance Typically a solid (color may vary depending on purity)
    Melting Point Specific value would require experimental determination
    Solubility Soluble in some organic solvents like dichloromethane
    Pka Data specific to this compound would need literature search
    Logp Value would depend on experimental determination or calculation models
    Stability Stable under normal storage conditions, but may react with strong oxidizing agents
    Hazard May cause skin, eye, and respiratory irritation

    As an accredited 1-{[(9H-Fluoren-9-Ylmethoxy)Carbonyl]Oxy}Pyrrolidine-2,5-Dione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 1-[(9H - Fluoren - 9 - ylmethoxy)carbonyl]oxypyrrolidine - 2,5 - dione in sealed vial.
    Shipping 1-{[(9H - Fluoren-9 - ylmethoxy)carbonyl]oxy}pyrrolidine - 2,5 - dione will be shipped in sealed, corrosion - resistant containers. Special care is taken to ensure compliance with chemical transportation regulations for safe transit.
    Storage 1 - [(9H - Fluoren - 9 - ylmethoxy)carbonyl]oxypyrrolidine - 2,5 - dione should be stored in a cool, dry place away from heat and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and contact with air, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions.
    Application of 1-{[(9H-Fluoren-9-Ylmethoxy)Carbonyl]Oxy}Pyrrolidine-2,5-Dione

    Controlling Racemization and β-Alanine Elimination in Multi-Ton Fmoc-Amino Acid Production

    In the manufacture of Fmoc-amino acids destined for solid-phase peptide synthesis (SPPS) under current Good Manufacturing Practice (cGMP), the critical process parameter window is defined by the competing demands of nucleophilic attack and base-catalyzed α-proton abstraction. When 1‑{[(9H‑fluoren‑9‑ylmethoxy)carbonyl]oxy}pyrrolidine‑2,5‑dione (Fmoc‑OSu) is charged to a chilled slurry of the unprotected amino acid in a water/dioxane mixture within a 2000 L glass-lined reactor, the exothermic carbamoylation must be managed so that the bulk temperature never exceeds 8 °C. A retreat-curve impeller operating at 75 rpm provides the low-shear mixing required to maintain a suspension of the fine amino acid crystals without inducing particle comminution that would later challenge the 12 μm sintered-metal inline filter during transfer to the crystallizer. The addition ratio of Fmoc‑OSu is held at 1.02–1.05 molar equivalents relative to the amino acid; exceeding 1.08 eq in the case of l-serine methyl ester hydrochloride derivatives triggers a measurable increase in the Fmoc‑β‑elimination byproduct, which generates dibenzofulvene and ultimately Fmoc‑dipeptide impurities that are inseparable by fractional crystallization. Simultaneously, the pH is adjusted and maintained at 9.2 ± 0.2 via metered addition of 20% w/w aqueous sodium carbonate, because excursions above 9.8 increase the racemization rate constant krac beyond 2.4 × 10−3 min−1 for phenylalanine derivatives, yielding l‑stereochemical purities below the 99.5% enantiomeric excess threshold required by the European Pharmacopoeia monograph for Fmoc‑l‑Phe‑OH (Ph. Eur. 10.8). Production-scale batches rely on a cascade control loop linking an in-situ attenuated total reflectance (ATR) FT‑IR probe tracking the carbamate carbonyl stretch at 1715 cm⁻¹ to the dosing pump for Fmoc‑OSu solution, allowing endpoint detection with a ±0.3% stoichiometric accuracy that eliminates the need for post-reaction scavenger resins. After phase separation of the aqueous layer, the organic phase is concentrated under reduced pressure in a wiped-film evaporator at 40 °C jacket temperature, and the crude Fmoc‑amino acid is crystallized from ethyl acetate/hexane in a forced-circulation crystallizer with a 3 K supersaturation control window to yield product with a residual dioxane level below 380 ppm (tested per USP <467>). The terminal articles are individual Fmoc‑l‑amino acids exceeding 99.7% HPLC purity (USP <621>) and 99.8% optical purity (USP <781>), supplied in batch sizes sufficient for multi-kilogram SPPS campaigns at pharmaceutical partners. The entire operation is audited against ICH Q7 Section 8.1 (Production and In‑Process Controls), with critical deviations logged electronically in a validated manufacturing execution system.

    Why Does Fmoc-OSu Stoichiometry Shift from 1.05 to 1.30 Equivalents in Peptide Fragment Cyclization?

    When a fully deprotected peptide fragment bearing multiple solvent‑exposed amino groups is treated with Fmoc‑OSu for selective Nα‑protection prior to side‑chain cyclization, the observed optimal stoichiometry diverges markedly from the canonical 1.05 eq used for single‑residue substrates. Industrial syntheses of cyclic pentapeptide intermediates for gonadotropin‑releasing hormone antagonists demonstrate that a 1.25–1.30 molar equivalents of Fmoc‑OSu are required to achieve quantitative conversion of the target primary amine in dimethylformamide (DMF) at −5 °C, because the competing consumption by histidine‑ε and lysine‑ε side‑chain ammonium ions—present in partial apo‑form under the 0.1% v/v diisopropylethylamine (DIPEA) base load—creates a kinetic sink that is absent in pure amino acid carbamoylation. The reaction is run in a jacketed cylindrical vessel equipped with a 4‑blade pitched‑turbine agitator at 200 rpm to disperse the Fmoc‑OSu solution added via a submerged dip pipe; failure to maintain a minimum tip speed of 1.2 m/s results in localized high‑concentration zones where Fmoc‑homodimerization of the peptide becomes detectable on LC‑MS above 0.15 area%. Production-scale batches adhere to ICH M7 guidelines for mutagenic impurities, necessitating that dibenzofulvene-byproduct levels stay below the threshold of toxicological concern (1.5 μg/day intake for a lifetime indication), which is controlled by limiting the post‑reaction hold time at basic pH to 30 minutes before quenching with 0.1 M KH₂PO₄. The protected fragment is isolated via precipitation from methyl tert‑butyl ether at −20 °C, washed with cold water to remove residual DIPEA‑HCl, and dried under a nitrogen sweep in an agitated filter‑dryer to achieve a Loss on Drying value of <0.5% (USP <731>). The terminal product is a single‑chain Fmoc‑protected peptide fragment with a defined cyclization handle, used as a late‑stage intermediate in solution‑phase convergent synthesis of peptidomimetic drug substances. Auditor-relevant documentation includes batch records demonstrating compliance with the API starting material designation under ICH Q11, supported by mass spectral identity testing per USP <736>.A production line processing a valine-citrulline linker construct for an antibody-drug conjugate (ADC) intended to target a solid-tumor antigen introduces a distinct set of environmental and chromatographic controls that are absent in conventional peptide manufacturing. The linker core, typically an MC‑Val‑Cit‑PABC peptide, requires temporary masking of the citrulline α‑amine before carboxylic acid activation and subsequent coupling to the self‑immolative para‑aminobenzyl alcohol spacer. Fmoc‑OSu is added at a precise 0.98–1.02 molar equivalent to the linker amine in anhydrous N‑methyl‑2‑pyrrolidone (NMP) containing 2.0 eq of 2,4,6‑collidine as a non‑nucleophilic base. The process is executed inside an ISO 14644‑1 Class 8 cleanroom environment with positive‑pressure differentials of 15 Pa relative to adjacent gray zones, because the Fmoc‑protected linker intermediate must meet endotoxin limits of <0.05 EU/mg and bioburden <1 CFU/100 mg prior to conjugation with the cytotoxic payload. The reaction is monitored offline by UPLC with a quantitation limit of 0.05 area% for the des‑Fmoc impurity; should the des‑Fmoc peak exceed 0.10 area%, the batch is rejected because the downstream maleimide‑cysteine coupling to the monoclonal antibody becomes stoichiometrically unpredictable, leading to drug‑to‑antibody ratio (DAR) heterogeneity beyond the specification window of 3.5–4.0. Purification involves loading the quenched reaction mixture directly onto a 30 cm inner‑diameter dynamic axial compression column packed with 10 μm C18 bonded silica, eluting with a gradient of acetonitrile/water containing 0.1% trifluoroacetic acid. The pooled product fractions are concentrated by tangential flow filtration through a 1 kDa molecular weight cutoff polyethersulfone membrane, lyophilized, and filled into borosilicate vials under a nitrogen headspace that maintains oxygen levels below 50 ppm. The terminal article is an Fmoc‑protected dipeptide linker intermediate with a residual solvent profile compliant with USP <467> Option 1 and a total impurity content below 1.0 area% as assessed by a validated stability‑indicating method. The master batch record cross‑references 21 CFR 210.22 and 211.22 for quality control unit responsibilities, confirming that the release testing includes elemental impurity screening per ICH Q3D, with cadmium, lead, and arsenic levels verified below 1 μg/g.

    When Poly(L‑lysine) Dendrimers Require Orthogonal Amine Protection for siRNA Complexation

    Functionalization of poly(L‑lysine) (PLL) dendrimers of generation 3 through generation 5 for non‑viral gene delivery vectors uses Fmoc‑OSu to transiently occupy a defined fraction of the pendant ε‑amino groups, enabling subsequent regioselective pegylation or targeting‑ligand conjugation. The degree of Fmoc substitution is controlled by adding 0.55–0.80 molar equivalents of Fmoc‑OSu per mol of primary amine in a DMF/water (60:40 v/v) system at 4 °C under vigorous stirring delivered by a magnetic‑drive overhead unit operating at 400 rpm. Inferior mixing or a solution viscosity exceeding 15 mPa·s causes inhomogeneous acylation that manifests as a bimodal particle size distribution after complexation with small interfering RNA (siRNA), shifting the polyplex z‑average diameter from the target 80–120 nm to a polydisperse population above 400 nm, as measured by dynamic light scattering at a backscatter angle of 173°. The partially Fmoc‑protected dendrimer is precipitated in cold diethyl ether, and residual Fmoc‑OSu hydrolyzate (pyrrolidine‑2,5‑dione and fluorenylmethanol) is reduced to ≤0.10 wt% by successive washes monitored by 1H‑NMR integration relative to the lysine‑ε‑methylene signal at 2.95 ppm. Industry‑compatible quality standards for this biomaterial intermediate include endotoxin specification <0.01 EU/μg (gel‑clot method referenced to USP <85>) and cytotoxicity screening against L929 fibroblasts in accordance with ISO 10993‑5, where cell viability must remain above 80% of the untreated control at a concentration of 1 mg/mL. The downstream process involves Fmoc removal with 20% piperidine in DMF, followed by PEG‑acrylate coupling to the exposed amines; the terminal product is a PEGylated PLL dendriplex‑forming polymer used in preclinical nucleic acid therapeutics. Equipment for the Fmoc‑OSu addition step is a disposable single‑use reactor bag with perfluoroalkoxy alkane (PFA)‑wetted temperature probes to prevent cross‑contamination with the cytotoxic siRNA payloads processed later in the same suite.Without an explicit header demarcation, the integration of Fmoc‑OSu into the synthesis of near‑infrared (NIR) cyanine‑dye‑labeled somatostatin analogs for intraoperative tumor imaging requires anchoring the fluorophore’s primary alkyl amine to the solid‑phase resin‑bound peptide backbone via a temporary Fmoc protection/deprotection cycle. In a representative process, a heptamethine cyanine derivative containing a 6‑aminohexanoic acid spacer is dissolved in anhydrous DMF and treated with 1.10 eq of Fmoc‑OSu in the presence of 2.5 eq of DIPEA at 22 °C for 90 minutes. The loading ratio is verified by fluorescence‑based quantitative HPLC, which must confirm a residual free‑amine content below 0.5% of the total dye peak area to avoid side reactions during subsequent coupling of the C‑terminus of the peptide to a chelator. Because the dye absorbs strongly at 780 nm, inadvertent exposure to ambient fluorescent lighting during Fmoc‑OSu addition accelerates photodegradation; manufacturing facilities therefore perform the reaction under red‑filtered LED illumination with a luminous flux not exceeding 5 lx at the vessel surface. Following aqueous workup and purification on a 100 Å pore‑size silica column using an isocratic elution of dichloromethane/methanol (97:3), the Fmoc‑protected dye‑linker construct is obtained as a dark‑green solid with purity ≥99.0% by peak area at the monitoring wavelength of 254 nm, adhering to internal release criteria derived from ICH Q3A(R2) for unspecified impurities. The terminal product is a dye‑spacer building block incorporated into automated Fmoc‑SPPS using standard activation protocols, ultimately giving a fluorescence‑guided surgery probe subject to the radiopharmaceutical preparation monograph of the relevant national pharmacopoeia when the peptide is additionally labeled with 68Ga.

    Radiotracer Chelator Intermediates and Metal‑Sensitive Stoichiometry Windows

    In the preparation of 1,4,7,10‑tetraazacyclododecane‑1,4,7,10‑tetraacetic acid (DOTA)‑conjugated peptides for positron emission tomography (PET) imaging with 68GaCl₃, selective masking of an aminoethyl linker pendant to the DOTA macrocycle with Fmoc‑OSu is the predominant route that enables orthogonal deprotection and metal‑free purification. The reaction is performed on a chromatographically pre‑purified DOTA‑ethylamine precursor, to which Fmoc‑OSu is added at exactly 1.20 eq in a 2:1 v/v mixture of acetonitrile and 50 mM sodium bicarbonate (pH 8.3). Any deviation below 1.15 eq results in residual free amine that chelates trace zinc(II) ions extracted from borosilicate glassware, forming a stable ternary complex that co‑elutes with the desired monoprotected DOTA species on C18 reverse‑phase HPLC and causes the final radiolabeling yield with 68Ga to drop below 65% (radio‑HPLC integration). Conversely, exceeding 1.25 eq of Fmoc‑OSu produces a bis‑Fmoc impurity in which the acetate arms of DOTA partially undergo Fmoc‑transfer, necessitating a preparative HPLC re‑purification step that extends the cycle time by 8 hours. The process is governed by the metal‑impurity control requirements of EP 9.0, general chapter 5.20 on elemental impurities, and the final Fmoc‑protected DOTA intermediate must present a signal for iron(III) below 2 ppm as measured by inductively coupled plasma mass spectrometry to preclude interference with the subsequent 68Ga radiolabeling. Production equipment for this high‑value intermediate consists of a glass fixed‑bed reactor loaded with borosilicate Raschig rings, functioning as a static mixer during Fmoc‑OSu addition, which eliminates metal‑particle shedding from impeller seals. The terminal compound, Fmoc‑DOTA‑AEEA‑OH, is a brick‑redetrahydrofuran solvate isolated by freeze‑drying at a shelf temperature of −30 °C and a chamber pressure of 50 μbar, and is shipped under argon to radiopharmacy cleanrooms worldwide for on‑site solid‑phase peptide elongation and subsequent radiolabeling under cGMP for PET tracer manufacturing (complying with 21 CFR 212).
    Comparative Process Parameters for Fmoc-OSu Application Across Downstream Sectors
    Application FieldTypical Molar Eq. Fmoc-OSuSolvent/Base SystemCritical Process LimitPrimary Release Standard
    Fmoc-Amino Acid (SPPS raw material)1.02–1.08Water/dioxane, Na2CO3 pH 9.2Enantiomeric excess ≥99.5%Ph. Eur. Fmoc-amino acid monograph
    Peptide fragment cyclization1.25–1.30DMF, DIPEA 0.1% v/vDes-Fmoc dimer ≤0.15 area%ICH M7 (mutagenic impurity control)
    ADC linker intermediate0.98–1.02NMP, 2.0 eq collidineEndotoxin <0.05 EU/mg21 CFR 211, ICH Q3D
    Poly(L-lysine) dendrimer0.55–0.80DMF/water, base‑freePolyplex Z‑avg ≤120 nmISO 10993‑5, USP ⟨85⟩
    NIR dye labeling intermediate1.10DMF, DIPEA 2.5 eqPhotodegradation avoided; ambient light <5 lxICH Q3A(R2) (unspecified impurities)
    DOTA radiometal chelator1.20Acetonitrile/50 mM NaHCO3 pH 8.3Residual free amine ≤0.2%, Fe<2 ppmEP 5.20, 21 CFR 212
    Regulatory and Quality Framework per Sector – Fmoc‑OSu Derived Intermediates
    SectorManufacturing StandardAnalytical Test (Method)Specification LimitEquipment Qualification Reference
    Fmoc-Amino AcidICH Q7, EU GMP Part IIHPLC purity (USP 621), specific rotation (USP 781)Purity ≥99.5%, [α]D20 within ±1.0° of referenceASME BPE reactor and crystallizer certification
    ADC Linker21 CFR 210-211, ICH Q7 Annex 13Endotoxin (USP 85), bioburden (USP 61)<0.05 EU/mg, <1 CFU/100 mgISO 14644-1 Class 8 cleanroom, HEPA filtration
    Biomaterial (PLL dendrimer)ISO 13485, ISO 10993-1Cytotoxicity (ISO 10993‑5), endotoxin (USP 85)Cell viability ≥80%, <0.01 EU/μgSingle‑use reactor qualification per ASTM E3079
    PET Tracer Intermediate21 CFR 212, EudraLex Vol. 4 Annex 3Elemental impurities (ICH Q3D), radio‑HPLCFe <2 ppm, radiochemical purity >95% after labelingGlass fixed‑bed reactor cleaned per ASTM G93
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    Certification & Compliance
    More Introduction

    Catalogued systematically as 1-{[(9H-fluoren-9-ylmethoxy)carbonyl]oxy}pyrrolidine-2,5-dione, the compound is functionally recognized as Fmoc-OSu, the succinimidyl ester of the base-labile 9-fluorenylmethyloxycarbonyl protecting group. With CAS registry 82911-69-1 and a molecular formula of C19H15NO5 (molecular weight 337.33 g·mol⁻¹), this white to off-white crystalline powder serves as the primary acylation vehicle for introducing the Fmoc moiety onto the α-amine of proteinogenic and non-proteinogenic amino acids. Its design displaces the need for handling the volatile, shelf-unstable Fmoc chloride in contemporary peptide synthesis workflows.

    Why is Fmoc-OSu Routinely Preferred Over Fmoc Chloride for Solution-Phase Derivatization?

    When amino acid Nα-protection is executed in aqueous-organic biphasic systems, the hydrolysis rate of the reagent becomes the critical process variable. Fmoc chloride, still encountered in legacy protocols, hydrolyzes rapidly at pH values above 7.0, forming the unreactive N-(9-fluorenylmethyl)carbamic acid and dibenzofulvene via β-elimination. This side pathway consumes the reagent and generates fulvene adducts that co-elute with the protected amino acid during reversed-phase HPLC monitoring. Under identical biphasic conditions (dioxane/10% Na2CO3, 0–5 °C), the succinimidyl carbonate ester resists nucleophilic degradation for a sufficient processing window—its half-life in 0.1 M aqueous carbonate at 0 °C exceeds 45 minutes, compared to less than 8 minutes for Fmoc-Cl. This kinetic differential permits controlled stoichiometry of 1.05–1.15 equivalents relative to the free amine, minimizing over-acylation and the need for post-reaction extraction of dibenzofulvene derivatives. Production-scale batches conducted in jacketed stirred-tank reactors with bottom-drain valves on 100–500 L scale routinely achieve ≥ 97% isolated yield of Fmoc-amino acids after a single trituration with methyl tert-butyl ether.

    No separate header precedes the discussion of reagent physical form, allowing this paragraph to open the handling comparison directly. Fmoc-OSu is delivered as a free-flowing crystalline solid with a bulk density that permits accurate gravimetric dispensing on analytical balances with 0.1 mg readability. Fmoc chloride, in contrast, is a low-melting solid (mp 62–64 °C) that sinters under ambient storage and requires solvent transfer for reproducible charge. The succinimidyl ester melts sharply at 150–155 °C (determined by differential scanning calorimetry per ASTM E794 at 10 °C·min⁻¹ heating rate) with no decomposition exotherm until above 180 °C, a thermal profile compatible with standard laboratory heating blocks during solvent evaporation post-coupling.

    Purity Specification Thresholds and Their Cascade Effect on Peptide Crude Profiles

    Automated solid-phase peptide synthesis (SPPS) operating with Fmoc/tBu chemistry is exceptionally sensitive to the purity of the incoming Fmoc protection reagent. A single condensation cycle on a resin-bound amine utilizes the Fmoc-amino acid rather than free Fmoc-OSu, but the preparation of those Fmoc-amino acid synthons is where the reagent’s trace impurity profile becomes embedded. The accompanying table maps the key quality parameters measured against standard analytical methods.

    ParameterSpecification LimitAnalytical MethodImpact of Off-Spec Value
    Assay (anhydrous, non-aqueous titration)≥ 99.0% (w/w)Perchloric acid titration in acetic acid, potentiometric endpointUnder-charge of Fmoc-OSu leads to incomplete amine protection; residual free amino acid reacts in subsequent coupling cycles, generating deletion sequences.
    Water content≤ 0.30%Karl Fischer coulometry, ASTM E203Water hydrolyzes the active ester to Fmoc-OH, which does not acylate the amine. Each 0.1% water increase reduces effective reagent molarity by approximately 0.3%, requiring empirical excess adjustment.
    Dibenzofulvene (DBF) content≤ 0.50% (area %)HPLC, C18 column, UV 266 nm, isocratic acetonitrile/water 70:30Pre-existing DBF forms adducts with the amine component, generating a piperidine-stable impurity that cannot be removed by washing and persists into the final peptide.
    Melting point150–155 °CCapillary method or DSC ASTM E794Depression below 148 °C indicates residual solvent (typically ethyl acetate or THF) or incomplete drying, correlating with inaccurate gravimetric assay.

    In peptide facilities operating under cGMP (21 CFR Part 210/211), a supplier’s certificate of analysis must reference an HPLC purity method that resolves Fmoc-β-alanine, a known rearrangement byproduct of the succinimidyl ester at elevated pH, from the main peak. Resolution of at least 2.0 between Fmoc-OSu and Fmoc-β-Ala-OH on a 150 × 4.6 mm, 3 µm C18 column is a typical acceptance criterion. Failure to control this impurity adds a β-alanine-terminated truncation to the peptide product, detected only by high-resolution mass spectrometry.

    Assessing Shelf-Life Under Tropical Storage Conditions

    Moisture ingress is the dominant degradation vector. Long-term stability data generated at 25 °C / 60% RH in sealed laminated aluminum pouches with desiccant sachets demonstrate assay retention above 99.0% over 24 months. Once the container is opened and the reagent is exposed to ambient humidity exceeding 50% RH, a measurable increase in free Fmoc-OH is detected within 72 hours by thin-layer chromatography (silica gel 60 F254, ethyl acetate/hexane 1:1). In facilities located in equatorial zones without controlled humidity suites, it is common practice to sub-aliquot the material into single-use vials under dry nitrogen in a glovebox maintaining < 10 ppm H2O prior to freezer storage at -20 °C. Re-warming to ambient temperature must be performed in a still-sealed container to prevent condensation; a 1 kg container requires approximately 4 hours to equilibrate before opening without surface moisture formation.

    Synthetic peptide production on microwave-assisted synthesizers (CEM Liberty Blue or Biotage Initiator+ Alstra) adds a thermal stress dimension. In pre-activation protocols where Fmoc-amino acids are generated in situ from the free amino acid and Fmoc-OSu in dimethylformamide at 50 °C, the reagent demonstrates thermal stability with less than 2% degradation after 30 minutes, as monitored by inline UV at 301 nm. However, combination with the hindered base N-methylmorpholine must be strictly sequential; simultaneous addition of base and Fmoc-OSu to the amino acid solution promotes rapid formation of the Fmoc-β-alanine rearrangement impurity, reaching 5–8% within 5 minutes. The prescribed order of addition is: dissolve amino acid and 1.0 equivalent of N-methylmorpholine, then add Fmoc-OSu in a single portion. This stands in contrast to Fmoc-Cl, which demands inverse addition (reagent to base) to avoid uncontrolled exotherms.

    Differentiation from 9-Fluorenylmethyl Succinimidyl Carbonate and Other Fmoc Donors

    The nomenclature similarity between Fmoc-OSu and 9-fluorenylmethyl succinimidyl carbonate (Fmoc-OSu is technically a carbonate, as the Fmoc oxygen attaches to the carbonyl forming a mixed carbonate with succinimide) requires clarification: the compound is a single defined chemical entity, not a mixture of isomers. Confusion sometimes arises with Fmoc-OBt (1-{[(9H-fluoren-9-ylmethoxy)carbonyl]oxy}benzotriazole), which is the benzotriazolyl analog. Fmoc-OBt exhibits higher reactivity due to the better leaving-group ability of the benzotriazole anion (pKa of HOBt ≈ 4.6 versus pKa of HOSu ≈ 6.0), but its preparation is less atom-economical and the reagent is less crystalline, complicating purification. Fmoc-OSu is the intermediate of choice when the mildest stable active ester is required, particularly for amino acids bearing side-chain functionalities sensitive to nucleophilic catalysis (e.g., the γ-carboxyl of Fmoc-Glu-OtBu, where OBt esters can promote pyroglutamate formation).

    In the context of orthogonal protection schemes, Boc-OSu (tert-butyl succinimidyl carbonate) is the acid-labile counterpart used in Boc-SPPS. Fmoc-OSu-generated protection withstands the trifluoroacetic acid cocktail used for side-chain deprotection and cleavage in Fmoc chemistry, while the Boc group is removed simultaneously under those conditions. This orthogonality is the structural basis for the widespread adoption of the Fmoc strategy in multi-kilogram production of generic therapeutic peptides such as leuprolide and goserelin. Process fits for these APIs routinely employ Fmoc-OSu-derived Fmoc-Leu-OH and Fmoc-Ser(tBu)-OH in fragment condensations on 50–200 mmol scale, where the crystalline nature of the reagent supports direct addition via solid dispensing systems without the line blockages experienced with hygroscopic oils.