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(2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 174999
    Product Name (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate)
    Common Name 2,3,4,6-Tetra-O-pivaloyl-α-D-glucopyranosyl bromide
    Cas Number 58477-73-7
    Molecular Formula C26H43BrO9
    Molecular Weight 579.52 g/mol
    Appearance White to off-white crystalline powder
    Physical State Solid
    Odor Odorless
    Purity ≥98%
    Grade Pharma Grade
    Assay 98.0% - 102.0%
    Solubility Soluble in organic solvents (chloroform, dichloromethane, ethyl acetate); insoluble in water
    Storage Conditions Store in a cool, dry place, away from light and moisture; recommended 2-8°C
    Shelf Life 24 months
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Packaging Amber glass bottle, double polyethylene bag, or as per customer requirement
    Hazard Classification Irritant
    Handling Precautions Use personal protective equipment; avoid inhalation and contact with skin/eyes

    As an accredited (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate) 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.

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    Application of (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Handling of (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl tris(2,2-dimethylpropanoate) in pharmaceutical manufacturing is constrained by two hydrolytically active sites: the C-2 bromide and the four pivaloyl ester groups. The tetra-O-pivaloylated bromosugar is supplied as a pharma-grade material, and the downstream routes described for tablet, capsule, granule, and injectable presentations are formulated under anhydrous or non-aqueous constraints because water, amines, and pH values above 5.0 accelerate solvolysis of the pivaloyl esters and the C-2 bromide. Published data for this specific configuration as a finished-dose API is limited; the numerical ranges cited below are representative formulation-platform starting points for perpivaloylated hexopyranose esters and require confirmation against specification batch data before filing.

    In dry-granulated immediate-release tablet campaigns, the compound is pre-screened through a 0.500 mm stainless steel mesh and conditioned at 20%–25% RH for not less than 4 h before weighing. The representative addition ratio uses 5.0% w/w pharma-grade bromosugar in a pre-blend of microcrystalline cellulose and anhydrous calcium hydrogen phosphate at a 1:4 ratio; croscarmellose sodium is split between intragranular 2.0% w/w and extragranular 1.0% w/w, and magnesium stearate is kept at 0.5% w/w with a 3 min final lubricant blend because higher shear ruptures the pivaloyl ester aggregates and increases surface energy. The downstream dry-granulation process uses a roller compactor at roll pressure 4–6 kN/cm and roll gap 1.0–1.5 mm, followed by screening through 0.800 mm and tableting at 15–25 kN with friability not exceeding 1.0% under USP <1216>. Lactose monohydrate should be avoided because surface water and reducing saccharide impurities can promote browning and C-2 bromide solvolysis; anhydrous dibasic calcium phosphate is preferred because its free-water content is below 0.1% w/w. Terminal finished product type: immediate-release tablet with a non-aqueous moisture-protective film coating, tested for disintegration not more than 15 min under USP <701>, content uniformity under USP <905>, and stability under ICH Q1A(R2).

    Lipid preconcentrate for hard capsules without aqueous granulation

    Hard-capsule filling of the lipophilic tetra-O-pivaloyl bromosugar uses a preconcentrate vehicle composed of medium-chain triglycerides, propylene glycol monocaprylate type II, and polyoxyl 35 castor oil. The representative fill blend is 10.0% w/w compound, 45.0% w/w polyoxyl 35 castor oil, 30.0% w/w propylene glycol monocaprylate, and 15.0% w/w medium-chain triglyceride; no aqueous phase is introduced because free water would generate pivalic acid through ester cleavage and convert the C-2 bromide to the corresponding hemiacetal. The downstream process consists of a jacketed high-shear mixer at 35–40°C, a 0.45 μm clarification filter, and liquid-fill capsule equipment with a fill weight of 450–500 mg into size 0 HPMC capsules that are immediately banded with HPMC/PEG 4000 at 55°C. Terminal product type: lipid-filled hard capsule. Compliance anchors include USP <711> for dissolution, USP <701> for disintegration, ICH Q3C for residual solvents, ICH Q3D for elemental impurities, and 21 CFR 211.166 for stability testing. The operational boundary is fill blend moisture not more than 0.2% w/w by Karl Fischer; capsule shells stored at 20–25°C and 40% RH to prevent shell cracking and retard pivaloyl ester hydrolysis at the fill-shell interface.

    When hydroalcoholic fluid-bed spraying is applied to reconstitutable granules

    Because the compound is sensitive to bulk water, fluid-bed granulation for oral sachet granules is run with ethanol containing not more than 10.0% water as the binder solvent; povidone K-30 is dissolved at 5.0% w/w of dry granule mass. The representative compounding ratio is 7.5% w/w compound, 85.0% w/w mannitol-microcrystalline cellulose blend at 1:1, 5.0% w/w povidone, 1.5% w/w crospovidone, and 1.0% w/w colloidal silicon dioxide. Equipment parameters are top-spray fluid-bed with inlet air 40–45°C, product temperature 28–32°C, atomizing pressure 1.2–1.8 bar, and spray rate 6–8 g/min per kg of substrate; final moisture is not more than 0.5% w/w. Terminal product type: reconstituted oral suspension after adding 10 mL purified water at the point of use, with a pH specification of 3.0–4.0 to reduce pivaloyl hydrolysis. Compliance includes USP <711>, USP <905>, ICH Q6A, and residual solvent limits for ethanol under ICH Q3C. The granular intermediate is packaged in foil-laminated sachets with desiccant and oxygen scavenger because residual moisture above 1.0% w/w reduces C-2 bromide content over 6 months at 40°C/75% RH.

    RouteCritical controlNumerical boundaryReference standard
    Dry-granulated tabletRoller compaction pressure4–6 kN/cmUSP <905>, USP <1216>, USP <701>
    Lipid-filled capsuleFill blend moisture≤0.2% w/wUSP <711>, ICH Q3C, ICH Q3D
    Reconstitutable granuleProduct temperature during fluid-bed spray28–32°CUSP <905>, ICH Q6A
    Injectable oil solutionWater content≤0.1% w/wUSP <71>, USP <85>, USP <787>
    Lyophilized injectionCake moisture≤2.0% w/wUSP <921>, USP <788>, ICH Q1A(R2)

    Injectable aseptic oil solutions are prepared by dissolving the compound in a non-aqueous vehicle of sesame oil and benzyl alcohol, with a target concentration of 20 mg/mL. The addition ratio of benzyl alcohol is held at 5.0% w/v because higher concentrations may extract container closure components and lower concentrations may allow microbial proliferation during hold time. The production process is aseptic filling from a 0.22 μm hydrophobic PVDF membrane filter into Type I glass ampoules under nitrogen, with fill volumes of 1.0 mL or 2.0 mL and terminal inspection for visible particles under USP <790>. Terminal product type: injectable oil solution for intramuscular depot administration, which uses the high partition coefficient of the tetra-O-pivaloyl ester to delay release. Compliance standards include USP <71> sterility, USP <85> bacterial endotoxin not more than 0.5 EU/mg, USP <787> subvisible particulate matter, USP <790>, and ICH Q3D. The boundary condition is water content not more than 0.1% w/w by USP <921>, because free water in the oil phase promotes anomeric bromide solvolysis and pivaloyl ester cleavage.

    What limits the primary drying shelf temperature for cyclodextrin-stabilized lyophilisates?

    For injectable lyophilisates, the compound is first complexed with sulfobutylether-β-cyclodextrin at a molar ratio of 1:20 in a 20 mM citrate buffer, pH 3.0, containing 2.0% w/v mannitol as a cryoprotectant. The representative pre-lyophilization ratio is 1 part compound, 20 parts cyclodextrin, 5 parts mannitol, and 74 parts citrate buffer; the high cyclodextrin ratio is required because the bulky pivaloyl ester occupies a large hydrophobic cavity volume and incomplete inclusion leads to reconstituted particle growth. The downstream production process uses a stainless-steel lyophilizer with a shelf cooling ramp of 0.5°C/min to -45°C, a hold of 180 min, primary drying at -25°C shelf temperature and 0.2 mbar chamber pressure for 30 h, and secondary drying at 25°C for 8 h. Terminal product type: sterile lyophilized powder for injection reconstituted with 0.9% sodium chloride to 5 mg/mL compound before intravenous administration. Compliance anchors are USP <71>, USP <85>, USP <921> moisture not more than 2.0% w/w, USP <788>, and ICH Q1A(R2). The lyophilizer load and edge-vial effect must be validated because supercooling differences greater than 5°C across the shelf alter cake collapse temperature and reconstitution time, producing vial-to-vial variability in residual moisture and the proportion of intact pivaloyl ester.

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    Competitive (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl Tris(2,2-dimethylpropanoate) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.

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    Certification & Compliance
    More Introduction

    The product (2R,3R,4S,5R,6R)-2-bromo-6-((pivaloyloxy)methyl)tetrahydro-2H-pyran-3,4,5-triyl tris(2,2-dimethylpropanoate), supplied under material code BTHP-PG-01 as a Pharma Grade API, is a single-stereoisomer protected glycosyl bromide with molecular formula C26H47BrO9 and molecular weight 583.55 g/mol. The material is controlled as a white to off-white crystalline powder and is designated for formulation screening in tablet, capsule, granule, and injectable presentations. No harmonized Ph. Eur., USP–NF, or JP monograph exists for this exact protected halide; release therefore follows an internal specification aligned with ICH Q3A, ICH Q3C, and ICH Q3D. The pivaloyl moieties at C-3, C-4, C-5, and the pivaloyloxymethyl substituent at C-6 provide steric shielding around the bromide-bearing carbon adjacent to the ring oxygen, moderating hydrolysis during solid-state processing while retaining electrophilic reactivity for subsequent glycosylation or substitution. Oral and injectable grades differ principally in bioburden, bacterial endotoxin, sterility, and subvisible particulate controls.

    Because the C–Br bond is activated toward nucleophilic displacement, aqueous and alkaline conditions must be excluded during handling. The pivaloyl ester groups are relatively stable at neutral pH but undergo saponification in strong base, releasing pivalate and the unprotected polyol. In formulation laboratories, the material is not combined with primary or secondary amines, alkoxides, carbonate bases, or aqueous buffers above pH 7.0. Handling at relative humidity above 60% or exposure to open air for more than 24 h may raise free water above the ≤0.5% w/w Karl Fischer limit and initiate agglomeration. Bulk containers are opened only under nitrogen or argon in a dry glovebox or isolator.

    Solid-state characterisation is performed by X-ray powder diffraction using Cu Kα radiation at 40 kV/40 mA; the powder pattern shows distinct crystalline reflections in the 5–35° 2θ range, but no published reference pattern is available for this exact structure. Particle size distribution is measured by laser diffraction according to ISO 13320:2020 or USP <429>. For oral tablet and capsule grades, the D90 is controlled between 75 µm and 150 µm; for injectable grades, jet milling under nitrogen is used to achieve D90 ≤10 µm. Micronization introduces amorphous surface domains, and the micronised powder is re-analysed by XRPD and Karl Fischer after 24 h equilibration at ≤30% RH. Differential scanning calorimetry at 10 K/min under nitrogen is used to detect low-melting impurities; however, thermal events may overlap with degradation, so interpretation is combined with thermogravimetric analysis and HPLC.

    What release and stability-indicating controls define this protected glycosyl bromide as pharma-grade?

    The release protocol combines identity, purity, and residual solvent measurements with route-specific microbial and particulate controls. The following table summarises the internal acceptance criteria for the oral-grade powder; the injectable grade applies the same chemical and enantiomeric purity limits but adds endotoxin and subvisible particle requirements.

    Quality attribute Acceptance criterion Test method/standard
    Appearance White to off-white crystalline powder Visual inspection
    Identity 1H NMR (400 MHz, CDCl3) and 13C NMR consistent with reference spectrum; HRMS [M+Na]+ within 5 ppm Ph. Eur. 2.2.33; in-house HRMS
    Assay by HPLC-ELSD ≥98.0% area ICH Q2(R2)-validated in-house method
    Individual unspecified impurity ≤0.10% area or ICH Q3A qualification threshold for intended dose ICH Q3A
    Total impurities ≤1.0% area ICH Q3A
    Water content ≤0.5% w/w Ph. Eur. 2.5.12 / USP <921>
    Residual solvents Class 1 and Class 2 solvents within ICH Q3C Option 1 limits Ph. Eur. 2.4.24 / USP <467>
    Sulfated ash ≤0.1% w/w Ph. Eur. 2.4.14 / USP <281>
    Elemental impurities ICH Q3D oral and parenteral limits Ph. Eur. 2.2.58 / USP <232>/<233>
    Bacterial endotoxins, injectable grade <0.10 EU/mg Ph. Eur. 2.6.14 / USP <85>
    Sterility, injectable grade Meets test for sterility Ph. Eur. 2.6.1 / USP <71>
    Particulate matter, injectable grade Meets USP <788> light obscuration limits for large- and small-volume injections USP <788>

    The HPLC-ELSD method employs a C18 stationary phase and an acetonitrile/0.1% trifluoroacetic acid gradient; ELSD is used because the pivaloyl ester has weak UV absorption. Forced degradation studies per ICH Q1A(R2) and ICH Q1B reveal that the main degradation pathways are hydrolysis of the bromide and de-esterification of the pivaloyl groups; the primary solid-state degradation products are the corresponding 2-hydroxy tetrahydropyran derivative and free pivalic acid. Published data for this specific configuration is limited, so the internal specification applies a total degradation product limit of ≤1.0% at release and requests lot-specific stability data for formulation batches.

    For tablet and capsule manufacturing, the crystalline powder is first delumped through a 0.5 mm stainless-steel screen and blended in a bin blender at 10–25 rpm for 10–15 min. The crystal habit is plate-like, and flow is typically poor; direct compression without flow additives is not recommended. Dry granulation by roller compaction is preferred over aqueous wet granulation because of the hydrolytic instability of the bromide. When roller compaction is used, ribbon density is maintained between 1.1 g/cm³ and 1.3 g/cm³, and the milled granule fraction between 0.150 mm and 0.710 mm is selected for compression. Tablet hardness values in development batches have been controlled in the 6–10 kp range, but these results are formulation-dependent and published data for this specific configuration is limited; each formulation must be verified by content uniformity and dissolution testing under USP <905> and USP <711> or Ph. Eur. 2.9.40 and 2.9.3.

    Capsule blending uses geometric dilution for low-dose strengths. The compound is compatible with lactose monohydrate, microcrystalline cellulose, crospovidone, and magnesium stearate in short blending cycles; alkaline lubricants such as sodium stearyl fumarate are not used without confirming pH control because pivalate hydrolysis is base-catalysed. Twin-screw extrusion above 45°C is not recommended because thermal elimination of pivalate esters may release isobutylene and pivalic acid. If a granule formulation is required, non-aqueous granulation with isopropanol and vacuum drying at 35–40°C has been used; residual solvent is confirmed by headspace GC before compression.

    When Pivaloylation Replaces Acetyl, Benzoyl, or Methoxyacetyl Protection in Oral and Injectable APIs

    The pivaloyl protecting group differentiates this API from acetyl-, benzoyl-, and methoxyacetyl-protected analogues. Acetyl esters are less sterically hindered and hydrolyse more rapidly in aqueous media; benzoyl esters introduce aromatic UV chromophores that simplify detection but tend to reduce crystallinity through π-stacking; methoxyacetyl esters provide greater polarity but are generally less stable under acidic conditions. Pivaloyl esters provide greater steric bulk, which reduces hydrolytic deprotection and improves crystallinity. The trade-off is increased lipophilicity and reduced aqueous solubility; injectable formulations therefore require a non-aqueous or surfactant-containing vehicle rather than simple phosphate-buffered saline at pH 7.4. Measured values for the partition coefficient of this exact compound are not available; fragment-based estimates indicate log P exceeds 5, but the value should be confirmed experimentally before final formulation design.

    Compared with unprotected or acetyl-protected glycosyl halides, the pivaloylated material is less hygroscopic and shows a lower tendency to undergo spontaneous elimination during storage at -20°C ± 5°C. However, the bromide remains reactive enough to require exclusion of thiols, azides, cyanide, and other strong nucleophiles from formulation components. The product is not interchangeable with acetyl-protected starting materials in synthetic routes without re-qualification of reaction stoichiometry, because the steric demand of the pivaloyl group alters glycosylation rates and stereochemical outcomes.

    For injectable presentations, the API is handled in an ISO 7 cleanroom under nitrogen overlay. Powder is dissolved in dimethyl sulfoxide or N-methyl-2-pyrrolidone and sterilised by membrane filtration through a 0.22 µm PVDF filter; terminal steam sterilisation is unsuitable because the C–Br bond is hydrolytically unstable at elevated temperature. Lyophilised formulations are prepared from tert-butanol/water mixtures with primary drying shelf temperature below -20°C to prevent melting and degradation. Residual water in the freeze-dried cake is controlled to ≤1.0% w/w by Karl Fischer titration. Subvisible particulate matter is controlled under USP <788>, and bacterial endotoxin is determined by Ph. Eur. 2.6.14/USP <85> with limits derived from the intended maximum bolus dose.

    Dosage form Critical attribute Acceptance criterion Control method
    Tablet Content uniformity AV ≤15.0 USP <905> / Ph. Eur. 2.9.40
    Capsule Microbial limits, non-sterile oral TAMC ≤103 CFU/g; TYMC ≤102 CFU/g Ph. Eur. 5.1.4 / USP <61>/<62>
    Granule Loss on drying ≤2.0% w/w USP <731> / Ph. Eur. 2.2.32
    Injection, solution Bacterial endotoxins <0.10 EU/mg or dose-based limit Ph. Eur. 2.6.14 / USP <85>
    Injection, lyophilised Residual water ≤1.0% w/w Ph. Eur. 2.5.12 / USP <921>

    Thermal Degradation and Residual Solvent Behaviour of the Protected Bromide

    Thermal stress is a critical processing boundary. Differential scanning calorimetry data for the exact compound are not publicly available; therefore, the material is handled with the conservative limit of 40°C for extended operations and 60°C for not more than 10 min. Above 60°C, pivalate esters can undergo thermal elimination, generating isobutylene and pivalic acid. The bromide itself can undergo debromination in the presence of iodide, phosphines, or tertiary amines; such reagents must not be present in formulation matrices. Residual solvent removal after granulation is carried out in a vacuum tray dryer at 35–40°C and 5–10 kPa; the bed depth is maintained below 2 cm to avoid moisture entrapment. Lot release includes headspace GC for isopropanol, tert-butanol, and methylene chloride according to ICH Q3C Option 1 limits.

    Storage stability is assigned a 12-month re-test date when the material is held at -20°C ± 5°C in sealed amber borosilicate vials under argon. Above 2–8°C, hydrolysis of the bromide accelerates; therefore, ambient storage is limited to 72 h for weighed portions in controlled low-humidity isolators. Repeated freeze-thaw cycles of open containers are not recommended because condensed moisture increases water content and promotes de-esterification.

    Operational boundaries are defined by the reactivity of the bromide and the base sensitivity of the pivalate esters. The API is incompatible with primary and secondary amines, alkoxides, strong aqueous bases, and metal hydrides. It is not milled in air at high energy for extended periods because electrostatic charging and local hot spots may generate pivalic acid. For oral solid dosage forms, the material is best processed by dry granulation or roller compaction at controlled humidity; for injectable forms, non-aqueous or low-water vehicles are required. Published data for this specific configuration is limited in the public domain; lot-specific certificates of analysis and route-specific qualification batches are required before commercial manufacturing.

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