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10-Deacetylbaccatin III(10-DAB) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: 10-Deacetylbaccatin III(10-DAB) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 772259
    Product Name 10-Deacetylbaccatin III (10-DAB) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Synonyms 10-DAB; 10-Deacetylbaccatin III; 10-Deacetyl Baccatin III
    Cas Number 32981-86-5
    Molecular Formula C29H36O10
    Molecular Weight 544.59 g/mol
    Appearance White to off-white crystalline powder
    Purity Assay ≥98.0% (HPLC)
    Grade Pharma Grade / GMP
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Solubility Soluble in methanol, ethanol, DMSO, chloroform; practically insoluble in water
    Melting Point 232-234 °C
    Storage Conditions Store at 2-8°C, protected from light and moisture, in a tightly sealed container
    Source Extracted from Taxus species or semi-synthetic
    Use Pharmaceutical intermediate/API for taxane derivatives such as paclitaxel and docetaxel
    Shelf Life 24 months when stored as recommended
    Packaging Double polyethylene bags in aluminum foil bag or fiber drum
    Loss On Drying ≤0.5%
    Residue On Ignition ≤0.1%
    Heavy Metals ≤10 ppm

    As an accredited 10-Deacetylbaccatin III(10-DAB) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 10-Deacetylbaccatin III (10-DAB) Pharma Grade API packed in 1 kg double-lined aluminum foil bags inside fiber drums for oral/injectable formulations.
    Container Loading (20′ FCL) 10-DAB Pharma Grade API loaded in 20′ FCL: securely palletized, moisture-protected drums, compliant labeling, optimized for safe oral/injectable pharmaceutical transport.
    Shipping 10-DAB Pharma Grade API is shipped in sealed, light-resistant, tamper-evident containers under controlled ambient or refrigerated conditions as required. Each consignment includes COA, MSDS, and customs documentation. Packaging complies with IATA/ADR/IMDG for safe international transport of oral and injectable-grade material. Temperature data loggers may be included where necessary.
    Storage Store 10-Deacetylbaccatin III (10-DAB) Pharma Grade API in a tightly sealed, light-resistant container under inert gas if required. Keep refrigerated at 2–8°C, dry, protected from moisture, heat, and light. Use in a clean, well-ventilated area separate from oxidizers. For oral and injectable use, maintain designated temperature, humidity, and contamination controls; follow labeled stability data.
    Shelf Life Typically 24–36 months if stored tightly sealed, protected from light, moisture, and heat; confirm exact retest date on supplier COA.
    Application of 10-Deacetylbaccatin III(10-DAB) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    For the manufacture of paclitaxel USP injectable concentrate, 10-deacetylbaccatin III (10-DAB) functions as the diterpene core for C13 side-chain attachment through a β-lactam coupling sequence. The incoming 10-DAB is treated as a GMP starting material under ICH Q7, with acceptance criteria routinely specified as HPLC purity ≥99.0% area, any single unspecified impurity ≤0.10%, and total impurities ≤1.0%. In the prevailing semi-synthetic route, the C7 hydroxyl is first converted to a triethylsilyl ether, after which the protected baccatin III intermediate is acylated with an activated N-benzoyl-β-phenylisoserine side chain. The molar proportion of 10-DAB to the side-chain precursor is typically set between 1.0 and 1.5 equivalents; published process descriptions favour a 1.2- to 1.3-fold excess of side chain to drive the C13 acylation to completion while suppressing dimerisation. The coupling is carried out in anhydrous dichloromethane or toluene under inert atmosphere at temperatures between −20 °C and +5 °C, using a tertiary amine base such as 4-dimethylaminopyridine or lithium hexamethyldisilazide. After coupling, the silyl protecting group is removed under mildly acidic conditions, and crude paclitaxel is purified by normal-phase silica gel chromatography followed by crystallisation from a solvent/anti-solvent system. Terminal product is paclitaxel USP API intended for concentrate for solution for infusion, typically formulated at 6 mg/mL in polyoxyethylated castor oil (Cremophor EL) and dehydrated ethanol. Final API compliance requires conformance to the Paclitaxel monograph in USP–NF or Ph. Eur., with assay 97.0%–102.0% on the anhydrous basis, total related substances not more than 2.0%, and residual solvents controlled under ICH Q3C Option 1 (for example, dichloromethane ≤600 ppm, methanol ≤3000 ppm). The terminal dosage form is an intravenous injection; no regulatory‑approved oral tablet, capsule, or granule presentation exists for paclitaxel because of first-pass metabolism and P-glycoprotein–mediated efflux. Production-scale hardware for this route typically uses glass-lined reactors of 500 L to 5000 L, with in-process control at the coupling step by thin-layer chromatography or HPLC to confirm that the residual protected 10-DAB derivative is below 0.5% before chromatographic purification. Batch-to-batch variability in the crystallisation step is a recurring bottleneck: uncontrolled cooling rates can produce paclitaxel with particle-size distributions outside the specification of downstream micronisation, and recovery of the silica gel from normal-phase chromatography adds solid-waste handling constraints that are not present in reversed-phase process variants.

    Why Does Docetaxel API Demand Anhydrous Reaction Controls?

    Semi-synthesis of docetaxel from 10-DAB exploits the same C13 hydroxyl acylation chemistry as paclitaxel, but the target molecule retains free hydroxyls at C7 and C10, and the side chain carries a tert-butoxycarbonyl protecting group on the amine. Reported routes frequently protect the C7 and C10 hydroxyls as silyl ethers or carbonates before C13 acylation, then remove these groups under conditions that do not hydrolyse the β-lactam side chain. The molar ratio of activated N-Boc-phenylisoserine to protected 10-DAB is held between 1.05 and 1.20, with the slight excess of side chain minimising the formation of the bis-acylated impurity. Anhydrous conditions are mandatory because water promotes premature deprotection of the Boc group and can reduce the yield of the final API below 85% in the coupling step. The reaction medium is typically tetrahydrofuran or dichloromethane dried over molecular sieves; residual water is specified at ≤0.01% by Karl Fischer titration in the reaction solvent. After coupling and deprotection, crude docetaxel is purified by preparative HPLC or by multiple recrystallisations from acetone/water. Terminal product is docetaxel anhydrous or docetaxel trihydrate API for injection concentrate, usually 20 mg/mL or 40 mg/mL, and also for lyophilised powder for solution for infusion. Compliance is anchored to the Docetaxel monograph in Ph. Eur. or USP, with assay 97.0%–102.0%, total impurities ≤2.0%, and elemental impurities below the limits in ICH Q3D for parenteral administration. Residual solvents are controlled per ICH Q3C; for example, tetrahydrofuran is limited to 720 ppm and dichloromethane to 600 ppm in the final API. As with paclitaxel, no oral dosage form of docetaxel has obtained marketing authorisation; the clinical literature attributes oral failure to CYP3A4 metabolism and intestinal P-glycoprotein efflux, not to a lack of API potency.

    Cabazitaxel Semi-Synthesis: Protecting Group Strategy and Final Deprotection

    Cabazitaxel is produced from 10-DAB by selective methylation of the C7 and C10 hydroxyl groups, followed by attachment of the same phenylisoserine side chain used in docetaxel. The methylating agent—commonly methyl iodide or dimethyl sulfate—is charged at 2.2–2.5 molar equivalents relative to 10-DAB in the presence of silver oxide or potassium carbonate to achieve complete dimethylation without over-methylating the C13 secondary alcohol. This protection step is run in polar aprotic solvents such as dimethylformamide or acetonitrile; dimethylformamide residue in the isolated intermediate must be controlled because it is an ICH Q3C Class 2 solvent. After methylation, the C13 hydroxyl is acylated under conditions similar to docetaxel, with the side-chain molar ratio maintained at 1.05–1.20 to prevent bis-acylation. Deprotection of the Boc group is carried out with trifluoroacetic acid in dichloromethane, and the final cabazitaxel API is purified by normal-phase chromatography or preparative HPLC. Terminal product is cabazitaxel concentrate for solution for infusion, typically 60 mg/1.5 mL in polysorbate 80 and ethanol, intended for intravenous use after dilution. Compliance requirements include ICH Q3C residual solvent limits for dimethylformamide (880 ppm) and dichloromethane (600 ppm), and ICH M7 control of mutagenic impurities because dimethyl sulfate is a potential genotoxic impurity; the corresponding acceptable intake is derived from compound-specific toxicology data. The API must meet a general assay specification of 97.0%–103.0% with total impurities ≤2.0%, as described in the manufacturer’s drug master file. Production hardware for the methylation step typically uses glass-lined or Hastelloy reactors because dimethyl sulfate is corrosive to stainless steel. The final injection is not available as a tablet or capsule, reflecting the established clinical limitation of oral taxane bioavailability rather than a formulation choice by the API manufacturer.

    Albumin-Bound Paclitaxel Manufacturing Imposes Tighter Residual Solvent Limits

    Nab-paclitaxel production begins with paclitaxel API derived from 10-DAB through the semi-synthetic route described above; the upstream molar ratio of 10-DAB to side-chain precursor is therefore identical to the paclitaxel mono, but the downstream paclitaxel must exhibit far stricter residual solvent control because the nanoparticle formulation is administered without further dilution of organic residues. In the standard process, paclitaxel is dissolved in a mixture of chloroform and ethanol, combined with an aqueous solution of human serum albumin, and subjected to high-pressure homogenisation at pressures up to 20,000 psi to form albumin-stabilised nanoparticles with mean particle size below 200 nm. Residual chloroform in the paclitaxel API is limited to ≤60 ppm per ICH Q3C, and residual ethanol to ≤5000 ppm, because the final lyophilised product is reconstituted with saline before infusion. Compliance for nab-paclitaxel is governed by both small-molecule and biologic requirements: the paclitaxel component must meet the USP Paclitaxel monograph, the albumin component must comply with FDA 21 CFR 601 for biological products, and the finished injection must pass USP <788> particulate matter and USP <790> visible particulate tests. Terminal product is sterile lyophilised powder for injectable suspension, 100 mg paclitaxel per vial, reconstituted with 20 mL of 0.9% sodium chloride. Equipment used in the homogenisation step includes microfluidizers with diamond interaction chambers; crevice corrosion in the high-pressure chamber is a known failure mode when chloride-containing residual solvents from upstream 10-DAB processing are present, so API suppliers are often requested to provide a chloride content certificate below 50 ppm. The downstream production line also requires aseptic filling and lyophilisation under Grade A conditions, which adds a separate cGMP burden relative to a conventional paclitaxel solution. No oral formulation of nab-paclitaxel is approved; the albumin carrier is designed for intravenous delivery, and oral administration would expose the paclitaxel to gastric degradation before absorption.
    Downstream Track Molar Ratio of 10-DAB to Key Reagent Critical Process Step Terminal Product Primary Compliance Anchor
    Paclitaxel API 1.0–1.5 eq side chain (typical 1.2–1.3) C13 acylation with β-lactam Injection concentrate 6 mg/mL USP/Ph. Eur. Paclitaxel, ICH Q3C
    Docetaxel API 1.05–1.20 eq N-Boc-phenylisoserine Anhydrous C13 coupling Injection concentrate 20 mg/mL / 40 mg/mL, lyophilised powder Ph. Eur. Docetaxel, ICH Q3D
    Cabazitaxel API 2.2–2.5 eq methylating agent C7/C10 dimethylation Injection concentrate 60 mg/1.5 mL ICH M7, ICH Q3C
    Nab-paclitaxel Same as paclitaxel route High-pressure homogenisation with albumin Lyophilised powder for injectable suspension 100 mg FDA 21 CFR 601, USP <788>
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    Certification & Compliance
    More Introduction

    10-Deacetylbaccatin III (10-DAB), CAS 32981-86-5, molecular formula C29H36O10, relative molecular mass 544.59 g/mol, is a taxane diterpenoid obtained from Taxus species by extraction and chromatographic purification. Pharma grade API is supplied as a white to off-white crystalline powder under manufacturer-specific lot codes that indicate the intended dosage-form route, particle size grade, and compendial test package. No harmonized international model number exists; the product is defined by the certificate of analysis, the extraction or semi-synthetic route, and the end-use quality level for tablet, capsule, granule, or injectable processing. The C-13 hydroxyl is the primary site for downstream side-chain coupling, while the free C-10 hydroxyl differentiates the molecule from baccatin III and influences chromatographic retention, chemical stability, and solubility behavior. The product is used either as an unconjugated API in formulations that specifically identify 10-DAB as the active moiety or as a purified taxane starting material; its acceptance profile should not be assumed equivalent to paclitaxel or docetaxel.

    How Is 10-Deacetylbaccatin III Characterized Against Impurity and Residual Solvent Monographs?

    Release testing for pharma grade 10-DAB is performed with a validated reverse-phase HPLC method on a C18 column using a water-acetonitrile gradient and UV detection in the range 227–230 nm. Identification includes infrared absorption concordance with a paired reference standard and HPLC retention time agreement. The acceptance criteria below are aligned with ICH Q3C, ICH Q3D, and relevant general chapters; manufacturer-specific specifications may be tighter for injectable use.

    ParameterAcceptance criterionReference method
    AppearanceWhite to off-white crystalline powderVisual, Ph. Eur. 2.2.2
    IdentificationInfrared spectrum concordant with reference standard; HPLC retention time concordantUSP <197K>, Ph. Eur. 2.2.24
    Assay by HPLC98.0–102.0% anhydrous, solvent-free basisValidated reverse-phase HPLC, UV 227–230 nm
    Baccatin III impurity≤0.5% areaHPLC
    7-epi-10-deacetylbaccatin III≤0.3% areaHPLC
    Any unspecified impurity≤0.10% areaHPLC
    Total impurities≤2.0% areaHPLC
    Loss on drying≤1.0%USP <731>, Ph. Eur. 2.2.32
    Sulfated ash≤0.1%USP <281>, Ph. Eur. 2.4.14
    Residual ethanol≤5000 ppmUSP <467>, ICH Q3C Class 3
    Residual methanol≤3000 ppmUSP <467>, ICH Q3C Class 2
    Residual dichloromethane≤600 ppmUSP <467>, ICH Q3C Class 2
    Elemental impuritiesComplies with ICH Q3D; route-specific daily dose limits applyUSP <232>, USP <233>
    Bacterial endotoxins≤0.5 EU/mg when injectable grade is specifiedPh. Eur. 2.6.14, USP <85>

    Residual solvent analysis is carried out by headspace gas chromatography with flame ionization detection; system suitability includes resolution between ethanol and methanol. Water content is determined by Karl Fischer titration with a precision of ±0.1%. Elemental impurities are assessed against ICH Q3D using inductively coupled plasma mass spectrometry after microwave digestion; limits depend on the intended daily dose and route of administration. For injectable-grade material, bacterial endotoxins and subvisible particulate matter are not optional tests; they are release specifications linked to the intended finished product claim.

    For method validation under ICH Q2(R1), specificity is demonstrated by separating 10-DAB from baccatin III, 7-epi-10-deacetylbaccatin III, and other process impurities. System suitability requires resolution between 10-DAB and 7-epi-10-DAB ≥1.5, tailing factor ≤2.0, and injection precision RSD ≤1.0% for five replicate injections. Detection and quantitation limits are set so that unspecified impurities can be reported at ≤0.05% area. Forced degradation is used to confirm that the method is stability-indicating; taxane diterpenoids are sensitive to C-7 epimerization under alkaline conditions and to oxidation at the C-10 hydroxyl. Published data for 10-DAB under all compendial stress conditions is limited and should be verified by LC-MS for the specific process route.

    Structurally, 10-DAB differs from baccatin III by the free C-10 hydroxyl; baccatin III carries a C-10 acetate ester and is therefore less polar. This difference reduces reversed-phase retention for 10-DAB and leaves the C-10 position available for subsequent acetylation or protection. 7-epi-10-deacetylbaccatin III is the C-7 epimer and is controlled as a related substance because incomplete resolution can inflate the 10-DAB assay. Paclitaxel and docetaxel contain the C-13 side chain that is absent in 10-DAB and are active anti-mitotic agents; 10-DAB cannot be substituted for these finished drug substances without validated side-chain coupling and purification. For operators purchasing 10-DAB as a tablet or capsule API, the specification should exclude baccatin III and 7-epi-10-DAB at the limits above and should confirm that particle size distribution, microbial quality, and residual solvents support oral dosage manufacture.

    When 10-DAB Is Processed Into Tablet, Capsule, and Granule Dosage Forms

    10-DAB is practically insoluble in water and exhibits cohesive powder flow; direct compression is therefore not recommended unless the active pharmaceutical ingredient is embedded in a coprocessed carrier. High-shear wet granulation in a 10 L bowl with aqueous binder solution is applied only after the API is pre-blended with a hydrophilic filler such as lactose monohydrate or microcrystalline cellulose. The granulation endpoint is monitored by impeller torque and product temperature; the wet mass is dried at 45–50°C to a loss on drying ≤2.0% before screening.

    For moisture-sensitive formulations, dry granulation by roller compaction is preferred. A roller compactor with side seals and a roll gap of 1.5–2.5 mm compacts the pre-blend; the ribbons are milled through a 1.0 mm screen. The resulting granules are blended in a bin blender with a fill volume of 50–70% and sampled at 10 locations to demonstrate blend uniformity with RSD ≤5.0%. Lubrication with magnesium stearate at 0.25–0.5% w/w is performed for 3–5 min to avoid over-lubrication.

    Tablet compression is conducted on a rotary tablet press to a hardness of 40–80 N and disintegration time ≤15 min according to USP <701>. Capsule filling using the same roller-compacted granulate follows mass uniformity and content uniformity testing under USP <905>. For granule-filled sachets, the granulate is sieved to 180–850 µm, and fines below 180 µm are limited to ≤20% to reduce segregation. Dissolution testing uses USP Apparatus II at 50–75 rpm with a surfactant-containing medium; published data for this specific configuration is limited and should be generated during formulation development.

    Particle size distribution is controlled by laser diffraction according to ISO 13320:2020. Oral-grade D90 is typically ≤50 µm, while micronized injectable-grade material is set at ≤10 µm when reduced aggregation and improved uniformity are required. Handling areas should be maintained below 60% RH because the free C-10 hydroxyl increases moisture interaction and can affect flowability. Pre-drying of excipients may be necessary when the relative humidity exceeds 60% for extended periods.

    Compared with baccatin III, 10-DAB may require additional protection against C-10 oxidation during wet granulation. The lower lipophilicity of 10-DAB relative to baccatin III changes the dissolution profile in surfactant media; in vitro testing should use a discriminating medium that meets USP <1092> solubility criteria rather than assuming the same surfactant concentration used for baccatin III. Gelatin capsule shells should be pre-conditioned below 45% RH because the API can retain moisture; hydroxypropyl methylcellulose capsules may be used when moisture sensitivity is observed.

    Injectable-Grade 10-DAB: Endotoxin, Particulate, and Solubility Constraints

    Injectable-grade lots are released with reduced bioburden, endotoxin control, and particulate matter testing. The API is dissolved in a non-aqueous or co-solvent system because of its practically insoluble aqueous solubility; ethanol, dimethyl sulfoxide, or a non-ionic surfactant-containing vehicle is selected only after compatibility screening with the free C-10 hydroxyl and the C-13 hydroxyl. The bulk solution is filtered through a 0.22 µm membrane and filled aseptically. Terminal steam sterilization is avoided unless thermal stability data for the specific solvent system are available; the taxane core is sensitive to hydrolytic degradation and C-7 epimerization in aqueous media above pH 6.0.

    Subvisible particulate matter is controlled according to USP <788>; visible particulates are inspected under Ph. Eur. 2.9.20. Bacterial endotoxins are tested with Ph. Eur. 2.6.14 or USP <85>; a limit of ≤0.5 EU/mg is commonly applied when the finished dosage form requires a pyrogen-free claim. Residual solvent levels for injectable use must satisfy ICH Q3C options based on daily exposure; methanol ≤3000 ppm and dichloromethane ≤600 ppm are baseline controls, but lower limits may be required for high daily doses. Closure compatibility is assessed by extraction studies under USP <381>, and vial headspace oxygen is controlled under nitrogen purging with a dissolved oxygen specification of ≤1.0 mg/L for oxidation-sensitive taxane formulations.

    For lyophilized injectable presentations, the fill solution is prepared under nitrogen and freeze-dried after aseptic filtration. The collapse temperature of the frozen formulation is determined by differential scanning calorimetry or freeze-drying microscopy; primary drying is set below the collapse temperature, and secondary drying is continued until cake moisture reaches ≤2.0% by Karl Fischer titration. The free C-10 hydroxyl in 10-DAB can alter the glass transition of the maximally freeze-concentrated solution relative to baccatin III; published data for this specific configuration is limited and should be established with formulation-specific thermophysical characterization. Any reprocessing from oral-grade to injectable-grade material is not recommended without validated purification, sterile filtration, and compliance with FDA 21 CFR 211.67 and 21 CFR 211.94.

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