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Di-tert-butyl Dicarbonate

    • Product Name: Di-tert-butyl Dicarbonate
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 395835
    Name Di-tert-butyl dicarbonate
    Cas Number 24424-99-5
    Molecular Formula C10H18O5
    Molecular Weight 218.25 g/mol
    Appearance Colorless liquid
    Melting Point -5 °C
    Boiling Point 155 °C (decomposes)
    Density 0.95 g/cm³ at 20 °C
    Solubility Soluble in organic solvents; insoluble in water
    Storage Temperature 2-8 °C

    As an accredited Di-tert-butyl Dicarbonate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Di-tert-butyl dicarbonate is packaged in sealed glass or HDPE bottles, available in quantities of 25 g, 100 g, and 500 g.
    Container Loading (20′ FCL) 20′ FCL: Di-tert-butyl dicarbonate loaded in sealed drums, secured, dry, ventilated, away from heat, moisture, and incompatible materials.
    Shipping Ship di-tert-butyl dicarbonate as UN 2920, Class 8 corrosive liquid with subsidiary Class 3 flammable risk, Packing Group II. Keep in sealed containers away from moisture and incompatible materials. Label with corrosion and flammable warnings; secure upright in ventilated packaging. Follow all applicable dangerous goods regulations for transport.
    Storage Store Di-tert-butyl dicarbonate in a tightly sealed container away from moisture, heat, and direct sunlight. Keep in a cool, dry, well-ventilated area, ideally under inert gas. Avoid contact with acids, bases, and oxidizers. Ensure the container is properly labeled and stored separately from incompatible materials.
    Shelf Life Di-tert-butyl dicarbonate has a shelf life of about two years when stored cool, dry, and tightly sealed away from moisture.
    Application of Di-tert-butyl Dicarbonate

    Di-tert-butyl dicarbonate CAS 24424-99-5, molecular weight 218.25 g/mol, is supplied as low-melting white solid with assay ≥99.0% w/w, water content by Karl Fischer titration ≤0.20% w/w, and melting range 22–24 °C. Industrial use is restricted to synthetic routes in which an acid-labile tert-butoxycarbonyl group is required to protect primary or secondary amines—or, less commonly, phenols—during subsequent processing. The following application scenarios are limited to verified downstream sectors: solid-phase peptide synthesis building blocks, small molecule pharmaceutical intermediates, photoresist polymer modification, agrochemical intermediate synthesis, heterobifunctional PEG linker manufacturing, and orthogonally protected unnatural amino acid derivatives.

    In solid-phase peptide synthesis, di-tert-butyl dicarbonate is introduced during the preparation of N-α-Boc-amino acid building blocks rather than as a direct deprotection reagent in Fmoc-mediated chain assembly. The reagent is charged at 1.05–1.30 mol per mole of free amino acid in a 1,4-dioxane:water 2:1 v/v solvent system, while the reaction temperature is maintained at 0–10 °C for the first 30–60 min and allowed to rise to 20–25 °C thereafter. The pH is held at 9–11 by controlled addition of 2.0 M aqueous sodium hydroxide; failure to maintain pH above 9 results in incomplete carbamoylation, while pH excursions above 11 accelerate hydrolysis of the reagent to tert-butanol and carbon dioxide. The exotherm and off-gassing profile on 500 L scale require jacket chilled-water supply at 2–5 °C and a vent line sized for 1.0–1.2 mol CO₂ per mole of dicarbonate consumed. After phase separation, the N-Boc amino acid is crystallized from ethyl acetate/heptane to yield material with residual starting amino acid below 0.5% w/w by HPLC area percent. Downstream, the N-Boc amino acid is used directly in Boc-protocol SPPS or in solution-phase peptide fragment coupling; for Fmoc-protocol SPPS, N-Boc amino acids are selectively deprotected and then Fmoc-protected after side-chain masking. Terminal peptide APIs produced through this route include therapeutic peptides requiring ≥98.0% chromatographic purity and residual trifluoroacetic acid below 0.1% w/w after lyophilization. Compliance requirements include ICH Q7 Section 8.1 for production controls, USP <467> for residual dioxane and heptane, and USP <621> for HPLC assay.

    Boc₂O charge (mol/mol amine)Reaction temperature after initiationTypical HPLC conversion at 4 h
    1.0520–25 °C96–98%
    1.2020–25 °C≥99%
    1.5020–25 °C≥99% but with higher Boc₂O-related impurities

    Why N-Boc Chiral Amine Intermediates Appear in Small Molecule API Manufacturing

    Within small molecule API campaigns, di-tert-butyl dicarbonate is charged to protected primary or secondary amines as a transient masking group enabling subsequent alkylation, reductive amination, or metal-catalyzed coupling to occur without N-functionalization side reactions. The reagent is added at 1.0–1.5 mol per mole of amine in anhydrous dichloromethane or tetrahydrofuran; when the substrate is poorly nucleophilic, 0.1–1.0 mol% 4-dimethylaminopyridine is co-charged and the mixture is stirred at 20–40 °C for 4–24 h. Use of a nitrogen atmosphere and pre-dried solvent is mandatory because residual water consumes dicarbonate and releases CO₂, causing pressure rise in closed reactors. On 200–2,000 L campaigns, reactor charging is performed with a solids addition system capable of 5–20 kg/h feed rate to avoid localized reagent concentration above 0.5 M; higher local concentration leads to symmetric urea side-product formation via reaction of the desired N-Boc intermediate with unreacted free amine. After washing with aqueous citric acid and brine, the intermediate is concentrated and carried forward or crystallized. Terminal products from such N-Boc intermediates are small molecule APIs, particularly oncology and antiviral compounds where the Boc-protected amine is deprotected with HCl/dioxane or trifluoroacetic acid and isolated as the hydrochloride or free base. Compliance controls follow ICH M7 for mutagenic impurity risk assessment of alkyl halide or urea side products, ICH Q3D for elemental impurities from metal catalysts, and USP <467> for residual dichloromethane and tetrahydrofuran. Analytical limits are set at ≤0.1% w/w for individual unknown impurities above the 0.10% identification threshold.

    When 4-hydroxystyrene/methacrylate copolymers are modified for chemically amplified DUV photoresist formulations, di-tert-butyl dicarbonate transforms pendant phenol groups into tert-butoxycarbonyl-protected phenols with acid-labile deprotection behavior. The post-polymerization modification is carried out in propylene glycol monomethyl ether acetate or tetrahydrofuran at 25–40 °C using 0.5–2.0 mol dicarbonate per mole of hydroxyl, with triethylamine or dimethylaminopyridine at 0.1–0.5 mol% as catalyst. The addition ratio is adjusted to a target blocking ratio because aqueous base solubility, glass transition temperature, and post-exposure bake deprotection temperature shift with degree of protection; partially protected polymers with 20–30 mol% Boc blocking exhibit clearing dose and contrast suitable for 248 nm lithography. After modification, the polymer is precipitated into hexane or heptane/water, filtered, and redissolved in PGMEA to 10–15 wt% solids. The downstream process includes filtration through 0.1 μm PTFE membrane and evaluation of dark film thickness loss, contrast curve, and line-space resolution. Terminal product is a chemically amplified photoresist polymer component supplied to resist formulators; it is not a formulated photoresist. Compliance obligations include REACH (EC) No 1907/2006 for EU market access, ISO 9001:2015 for lot traceability, and ISO 14644-1:2015 Class 5 cleanroom handling because trace metallic impurities must be below 100 ppb for sodium, iron, and chromium by ICP-MS to prevent gate oxide degradation. Published data for specific lithographic performance at sub-100 nm nodes is limited for this exact polymer modification route because resist evaluation is formulation-specific.

    Transient Amine Masking in Agrochemical Intermediate Synthesis

    Agrochemical routes to pyrazole carboxamide, aminopyrimidine, or thiazole-containing active ingredients frequently protect a primary aromatic or heterocyclic amine before halogenation, sulfonylation, or palladium-catalyzed cross-coupling. Di-tert-butyl dicarbonate is charged at 1.0–1.2 mol per mole of amine in tert-butanol or dichloromethane with 1.0–1.2 mol sodium bicarbonate or triethylamine; the reaction is run at 25–40 °C for 12–24 h under nitrogen. Off-gassing of CO₂ must be vented, and the headspace is monitored for pressure excursions on sealed reactors above 50 L capacity. The resulting N-Boc heterocyclic amine is carried into downstream steps without isolation, followed by acidic deprotection using HCl in dioxane or aqueous methanesulfonic acid to regenerate the free amine. Terminal products are agrochemical active ingredients, primarily fungicidal and herbicidal actives in the pyrazole and pyrimidine classes. Regulatory compliance for the intermediate and final active ingredient follows EU REACH and, for products exported to North America, EPA 40 CFR Part 180 residue chemistry data requirements for food-use crops; the manufacturing site typically applies ISO 14001:2015 environmental management because aqueous workup generates bicarbonate/tert-butanol waste streams. Residual tert-butanol in the isolated intermediate is controlled to below 0.5% w/w by GC headspace per internal specification aligned with USP <467> method formats.

    Aminofunctionalized monomethoxy poly(ethylene glycol) with molecular weight 2,000–5,000 Da is commonly produced with a tert-butoxycarbonyl-protected amine during chain extension and activation steps. Di-tert-butyl dicarbonate is introduced at 1.5–2.0 mol per mole of terminal primary amine in a dichloromethane/water biphasic mixture buffered with sodium bicarbonate to pH 8–9 at 20–25 °C for 6–18 h. Excess reagent is used because PEG-bound amines exhibit lower reactivity than small molecule amines and because moisture absorbed in the PEG matrix consumes dicarbonate. After phase separation, the Boc-protected PEG amine is isolated by precipitation in methyl tert-butyl ether at −10 to 0 °C and dried under vacuum at 25 °C to water content below 0.10% w/w. The protected intermediate undergoes further transformation—heterobifunctional carboxylation, maleimide introduction, or NHS-ester activation—before final Boc deprotection under trifluoroacetic acid/dichloromethane 50% v/v to release the free amine. Terminal product types include amino-PEG carboxylic acids, maleimide-PEG-amine linkers, and biotin-PEG-amine conjugates produced as both disperse and chromatographically purified single chain-length grades used in downstream bioconjugation and diagnostic reagent manufacturing. Compliance for these derivatives follows ISO 13485:2016 where contract manufacturers serve medical device and IVD component supply chains, and ICH Q7 when the linkers are used in clinical-stage antibody-drug conjugate manufacture. Lot release includes MALDI-TOF mass spectrometry for molecular weight distribution, 1H NMR for Boc group content, and USP <467> headspace GC for residual methyl tert-butyl ether and dichloromethane below pharmacopeial limits.

    When Unnatural Amino Acid Crystallization Requires Orthogonal Protection

    When β-amino esters, N-methyl amino acids, or constrained bicyclic amino acid scaffolds are manufactured for peptide mimetic and medicinal chemistry programs, N-Boc protection is selected because the tert-butoxycarbonyl group remains stable during ester hydrolysis, reductive alkylation, and hydrogenolysis steps that cleave benzyl or Cbz groups. Di-tert-butyl dicarbonate is introduced at 1.0–1.2 mol per mole of amino ester in tetrahydrofuran with 1.0–1.5 mol sodium bicarbonate and stirred at 0–25 °C for 8–16 h. Lower temperatures are used for β-amino esters prone to base-catalyzed retro-Michael elimination; the exotherm is controlled by adding the reagent in 0.2–0.5 mol portions, and the reaction is monitored by HPLC to avoid overprotection of unprotected hydroxyl groups. The downstream process isolates the N-Boc amino acid by solvent exchange to methyl tert-butyl ether, washing with 10% w/v aqueous citric acid, and crystallization from n-heptane/ethyl acetate. Terminal products are orthogonally protected amino acid derivatives, including N-Boc-trans-β-amino precursors and N-Boc-N-methyl amino acids, supplied to peptide synthesizers and CDMO laboratories. Compliance is governed by ICH Q7 for later API intermediate use, and analytical release includes chiral HPLC per USP <621> with enantiomeric excess above 99.0% and achiral HPLC purity above 98.0%. The operational boundary is strict: residual water above 0.5% w/w in the solvent system reduces yield and increases turbidity of the final crystallization because tert-butanol and di-tert-butyl carbonate hydrolysis products persist in the mother liquor.

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    Certification & Compliance
    More Introduction

    Di-tert-butyl dicarbonate (C10H18O5; CAS 24424-99-5; MW 218.25 g/mol) is a low-melting protecting reagent supplied as a white to off-white crystalline solid below 22.0 °C and as a clear liquid above 30 °C. The melting range specified under USP <741> is 22.0–24.0 °C, the boiling range is 56–57 °C at 0.5 mmHg, and the density is approximately 0.95 g/cm³ at 20 °C. The compound is soluble in dichloromethane, tetrahydrofuran, methyl tert-butyl ether, and tert-butanol; water contact generates carbon dioxide and tert-butanol. Representative catalogue grades include 205249 (Sigma-Aldrich) and B2045 (Tokyo Chemical Industry), but model codes are supplier-specific and do not replace the lot-specific certificate of analysis.

    Supplier specifications for a reagent-grade lot commonly require assay ≥99.0% by GC-FID using USP <621> system suitability, water content ≤0.50% by USP <921>, and residual solvent profile consistent with ICH Q3C and USP <467>. Tert-butanol is the predominant residual solvent and hydrolysis marker; typical acceptance thresholds are ≤0.50% w/w for peptide-grade material. Because the melting point brackets common laboratory ambient temperatures, drums may be received partially molten. Sampling from a single phase can under-report hydrolysis markers; homogenization at 28–30 °C under nitrogen with low-shear recirculation is therefore used before sampling from 50 L drums.

    What Limits the Assay Window When Moisture Ingress and Thermal Cycling Occur?

    Assay reproducibility is governed by post-receipt storage rather than the initial supplier certificate. Sealed containers stored at 2–8 °C typically remain within the ≥99.0% assay specification over a supplier-stated retest interval of 12 months; published degradation kinetics for opened containers under humid conditions remain limited because hydrolysis is headspace-transport controlled. Moisture ingress above 0.5% w/w generates tert-butanol and carbonic acid species, broadening the melting point to 19–24 °C and reducing the effective stoichiometric equivalent. On a 20–50 L glass-lined reactor line, material with water content above 1.0% w/w has been associated with 4–7 percentage-point lower isolated yield for N-Boc protection of hindered secondary amines, because the liberated tert-butanol competes with the substrate for reactive carbonyl species and CO2 absorption alters pH control. QC re-assay under ISO 17025 is therefore triggered after storage excursions above 30 °C or after exposure to relative humidity >60% for more than 4 h. Differential scanning calorimetry of aged technical material shows a broadened endotherm and a low-temperature exothermic shoulder; published calorimetric data for specific supplier grades are too sparse to establish a universal shelf-life limit.

    Slow Addition and pH Control for N-Boc Protection of Amino Acid Esters

    The primary application of di-tert-butyl dicarbonate is introduction of the tert-butyloxycarbonyl group onto primary and secondary amines, especially amino acid esters and solution-phase peptide intermediates. In a representative preparative protocol, 1.05–1.20 mol of di-tert-butyl dicarbonate per mole of free amine is added to a 0.2–0.5 M solution of the substrate in dichloromethane or tetrahydrofuran at 0–25 °C. Sodium bicarbonate or triethylamine at 1.0–1.5 equivalents maintains pH 8.5–10.0 and scavenges liberated tert-butanol. Under these conditions, N-Boc amino acid esters are isolated in 90–97% yield, with the symmetrical urea side product held below 3% by maintaining solvent water below 0.2% w/w. The reaction is exothermic and produces 1 mol of CO2 per amine equivalent; venting through a 2 M sodium hydroxide scrubber prevents pressure buildup in a 10–20 L jacketed reactor. For free amino acids, the protocol shifts to an aqueous-organic biphasic system, typically water–dioxane with sodium carbonate at 0–10 °C, and the N-Boc amino acid is isolated after pH adjustment to 2–3. For hindered substrates such as 2,2,6,6-tetramethylpiperidine, reaction completion requires 35–50 °C and 12–24 h; urea formation rises to 8–15% unless the addition rate is controlled below 0.05 mol/min per kilogram of substrate and the jacket temperature is held at −5 to 5 °C during the initial exotherm. In continuous-flow peptide synthesis, molten feed lines are maintained at 28–32 °C to avoid solidification in dead legs; the main process risk is CO2 pressure accumulation when the base pump lags, and pH excursions below 8.0 should trigger an interlock. In the presence of 4-dimethylaminopyridine, di-tert-butyl dicarbonate also converts primary and secondary alcohols to tert-butyl ethers, requiring 1.5–2.0 equivalents in dichloromethane at 20–40 °C.

    Compared with tert-butyl chloroformate, di-tert-butyl dicarbonate does not release hydrogen chloride during protection, eliminating the need for additional base to neutralise acid and reducing corrosion in stainless steel and glass-lined reactors. Its higher molecular mass 218.25 g/mol versus 136.58 g/mol raises reagent mass intensity by 59.8% per equivalent, but the byproduct profile is simpler because no chloride salt is formed. Compared with benzyl chloroformate, the Boc group is cleaved under acid conditions rather than by hydrogenolysis; this avoids palladium-catalyst cost and hydrogen handling but generates TFA or HCl waste streams. Compared with Fmoc chloride, the N-Boc group lacks the fluorenyl chromophore, so direct UV detection at 254 nm is less sensitive and preparative HPLC monitoring shifts to charged aerosol or mass detection. The protecting-group mass added to the substrate is 101.12 g/mol for Boc, 135.14 g/mol for Cbz, and 223.25 g/mol for Fmoc, which affects process mass intensity in multi-step peptide synthesis.

    ReagentCASMW (g/mol)Added protecting group mass (g/mol)Protection byproductsRepresentative cleavage
    Di-tert-butyl dicarbonate24424-99-5218.25101.12CO2, tert-butanol4 M HCl/dioxane or 50% TFA/DCM
    tert-Butyl chloroformate24608-52-4136.58101.12HCl, tert-butanolAcidolysis
    Benzyl chloroformate501-53-1170.59135.14HCl, benzyl alcoholH2/Pd-C hydrogenolysis
    Fmoc chloride28920-43-6258.70223.25HCl, dibenzofulvene/fluorenylmethanol20% piperidine/DMF

    When Di-tert-butyl Dicarbonate Replaces Benzyl Chloroformate in Multi-Kilogram Batch Hydrogenation

    For an intermediate bearing a halogenated aromatic ring that undergoes hydrodehalogenation under Pd/C hydrogenolysis, Cbz removal is not viable. N-Boc protection with di-tert-butyl dicarbonate is selected because the tert-butyloxycarbonyl group can be removed with 4 M HCl in dioxane or 50% TFA in dichloromethane at 0–25 °C without a hydrogenation step. The change eliminates the hydrogenation vessel and palladium filtration skid but requires a glass-lined deprotection vessel with scrubber capacity for isobutylene and carbon dioxide. Process records from 50–100 L glass-lined reactors show that linear N-Boc amines reach >99% conversion within 2 h at 20 °C in 4 M HCl/dioxane; hindered N-Boc amino acids require 25–35 °C and 4–6 h. Off-gas vent sizing must account for 1 mol of gas per mole of Boc group removed, plus the HCl vapour pressure of the dioxane solution. Relief devices on such vessels are typically set to 0.5 bar overpressure and connected to a caustic scrubber maintained at pH 12–13.

    Thermal Decomposition and Pressure Relief Scenarios in Bulk Storage

    Di-tert-butyl dicarbonate is thermally labile above 60 °C and should not be stored adjacent to steam tracing or heating jackets. Differential scanning calorimetry of technical-grade material shows an exothermic decomposition onset near 75–85 °C, depending on purity and container material, with gas evolution sufficient to overpressure a sealed 200 L drum if the closure does not vent. Supplier safety data sheets recommend storage at 2–8 °C in vented or pressure-relief containers; glass or HDPE containers with 1–2% headspace are standard in laboratory stockrooms. The compound has a closed-cup flash point of 37 °C and is classified as flammable under the Globally Harmonized System. Transfer of molten material above 30 °C requires grounding and bonding under EN 60079-14 area-classification practice. Hydrolysis in water releases 2 mol of CO2 per mole of di-tert-butyl dicarbonate, a stoichiometric basis for vent sizing during accidental wetting. Incompatibilities include strong bases, concentrated aqueous acids, and powdered metals; contact with concentrated aqueous ammonia causes rapid hydrolysis and vigorous gas release. Nitrogen inerting at ≤0.5 bar and sloped transfer lines prevent static liquid hold-up in dead legs.

    Table 2 consolidates the release specification for a typical peptide-synthesis grade. The limits are supplier-specific and may be tightened for pharmaceutical intermediates.

    ParameterMethodTypical acceptance limit
    AppearanceVisual examinationWhite to off-white crystalline solid or clear liquid
    AssayGC-FID, USP <621>≥99.0%
    Melting rangeUSP <741>22.0–24.0 °C
    Water contentKarl Fischer, USP <921>≤0.50%
    Residual tert-butanolHeadspace GC, USP <467>≤0.50%
    Residual Class 3 solventsICH Q3C / USP <467>≤5000 ppm
    Flash point, closed cupASTM D9337 °C

    Use of this specification is appropriate for laboratory-scale protection and pilot-kilo campaigns; production-scale peptide synthesizers may require additional particulate and endotoxin controls depending on the final API route and the relevant pharmacopoeial monograph.

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