| HS Code | 232658 |
| Product Name | (2R,3R,4R,5S,6S)-2-(Acetoxymethyl)-6-(4-chloro-3-(4-ethoxybenzyl)phenyl)tetrahydro-2H-pyran-3,4,5-triyl triacetate |
| Chemical Name | [(2R,3R,4R,5S,6S)-3,4,5-triacetyloxy-6-[4-chloro-3-[(4-ethoxyphenyl)methyl]phenyl]oxan-2-yl]methyl acetate |
| Synonyms | Dapagliflozin tetraacetate; Dapagliflozin tetraacetyl |
| Cas Number | 461432-25-7 |
| Molecular Formula | C29H33ClO10 |
| Molecular Weight | 577.02 g/mol |
| Appearance | White to off-white crystalline powder |
| Assay | ≥98.0% (HPLC) |
| Solubility | Soluble in dichloromethane, acetone, ethyl acetate; practically insoluble in water |
| Melting Point | 165-170°C (approximate) |
| Storage Conditions | Store at room temperature in a dry, well-ventilated area, protected from light and moisture |
| Pharmaceutical Grade | Pharma Grade API |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Routes Of Administration | Oral, Injectable |
| Stereochemistry | (2R,3R,4R,5S,6S) |
| Loss On Drying | ≤0.5% |
| Heavy Metals | ≤20 ppm |
| Residue On Ignition | ≤0.1% |
| Residual Solvents | Complies with ICH Q3C limits |
As an accredited (2R,3R,4R,5S,6S)-2-(Acetoxymethyl)-6-(4-chloro-3-(4-ethoxybenzyl)phenyl)tetrahydro-2H-pyran-3,4,5-triyl triacetate 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 | Supplied in 25 kg double-lined fiber drums with sealed LDPE inner bags, securely labeled Pharma Grade API for oral/injectable use. |
| Container Loading (20′ FCL) | 20′ FCL container loading: palletized, sealed pharma-grade API drums, loaded under temperature-controlled conditions for oral and injectable applications. |
| Shipping | Pharma Grade API shipped in sealed, tamper-evident, light-resistant containers. Store at controlled temperature, protect from moisture. Classified non-hazardous under IATA/IMDG/ADR unless otherwise specified. Packaging: double LDPE bags in HDPE drums. Include CoA, SDS, batch/expiry. For tablet/capsule/granule/injection, oral and injectable use. |
| Storage | Store in a cool, dry, well-ventilated area at 15–25°C, protected from light, moisture, heat, and incompatible oxidizers. Keep in tightly closed, original, labeled containers; use inert atmosphere if specified. For injectable grade, maintain sterility, endotoxin control, and cGMP compliance. Avoid freezing unless stability data support it. Follow supplier SDS and retest requirements. |
| Shelf Life | Typically 24–60 months for pharma-grade API stored sealed, light-protected, at controlled room temperature; protect from moisture/heat. Verify by stability data for oral/injectable. |
Within direct compression of low-dose oral SGLT2 inhibitor tablet development, the acetylated tetraacetate requires dry processing because residual free water above 0.5% w/w initiates ester hydrolysis in the presence of alkaline lubricants. When the tetraacetate is retained in the final dosage form as a protected intermediate for subsequent deacetylation, a parent empagliflozin equivalent of 10 mg corresponds to 13.7 mg tetraacetate based on the molar mass correction factor 1.373 (619.08 g/mol divided by 450.91 g/mol), yielding 13.7% w/w in a 100 mg core. For a 25 mg parent equivalent, 34.3 mg tetraacetate in a 150 mg core gives 22.9% w/w. Blending is performed in a 50 L bin blender at 25 rpm for 15 min, with microcrystalline cellulose and croscarmellose sodium pre-screened through a 500 μm mesh before the API is added; magnesium stearate lubrication is limited to 0.5 wt% and a final 3 min cycle because overlubrication of the needle-shaped acetylated particles lowers compact tensile strength below 1.5 MPa. Compression on a rotary tablet press with 8 mm round biconvex tooling uses precompression force 2.5 kN and main compression force 8–12 kN; tablet hardness is held at 6–10 kp and disintegration under USP <701> is ≤15 min. Compliance is anchored to USP <905> uniformity of dosage units with acceptance value ≤15.0, Ph.Eur. 2.9.5 uniformity of content, and FDA 21 CFR 211.110 in-process blend uniformity. The terminal finished product is an immediate-release film-coated tablet, and the processing boundary is a relative humidity below 40% to prevent particle agglomeration and ester hydrolysis during manufacturing.
| Parameter | 10 mg parent equivalent | 25 mg parent equivalent |
|---|---|---|
| Tetraacetate mass per core | 13.7 mg | 34.3 mg |
| Total core weight | 100 mg | 150 mg |
| API proportion | 13.7% w/w | 22.9% w/w |
| Microcrystalline cellulose | 70.0 mg | 90.0 mg |
| Croscarmellose sodium | 3.0 mg | 5.0 mg |
| Magnesium stearate | 0.5 mg | 0.75 mg |
| Hardness range | 6–8 kp | 8–10 kp |
| Disintegration USP <701> | ≤15 min | ≤15 min |
High-humidity exposure during dosator-type capsule filling of the tetraacetate creates a measurable shift in fill weight variability because acetate hydrolysis yields the free hydroxylated aglycone, which exhibits higher surface energy and cohesiveness on gelatin or HPMC shell walls. For low-dose capsules containing 0.5–10 mg parent-equivalent per size 3 HPMC shell, the tetraacetate addition is 0.7–13.7 mg in a total fill weight of 120 mg, corresponding to 0.6–11.4% w/w; the blend is prepared by geometric dilution of the API with lactose monohydrate pre-sieved through a 500 μm screen and blended in a 50 L V-blender at 30 rpm for 20 min. Powder bed humidity is controlled below 35% RH and the capsule filling room is maintained at 21 ± 2 °C because high atmospheric moisture accelerates acetyl ester hydrolysis; published kinetic data for this specific tetraacetate is limited, but the processing limit is set below 40% RH to maintain blend stability. Dosator pin compression is set to 0.5 bar with a pin height of 5.5 mm; weight variation acceptance is ±7.5% for a 120 mg fill and content uniformity is confirmed by Ph.Eur. 2.9.6 and USP <905>. The terminal finished product is a hard HPMC capsule, and the humidity boundary is the dominant operational limitation.
Roller-compacted dry granulation of the tetraacetate bypasses the hydrolytic degradation that occurs when water-based granulating fluid is sprayed at 5.0–8.0 wt% onto a starch-lactose substrate. In this downstream application, the API is required for single-dose oral granules where the parent-equivalent dose is 12.5 mg per 500 mg sachet, corresponding to 17.2 mg tetraacetate, or 3.4% w/w; the intra-granular blend is composed of pregelatinized starch, mannitol, and crospovidone at a 1:2:0.05 mass ratio. The dry granulation step uses a roller compactor with 25 mm knurled rolls at a gap of 1.5 mm and hydraulic pressure 60 bar; ribbon density is held at 1.1 g/cm3 before the slug is passed through an oscillating granulator fitted with a 0.8 mm screen. The resulting granules are lubricated with 0.5 wt% sodium stearyl fumarate for 5 min in a bin blender at 12 rpm, then filled into cold-seal aluminium sachets at 40% RH. Release specifications follow Ph.Eur. 2.9.12 sieve test and USP <786> analytical sieving; ICH Q1A accelerated stability at 40 °C/75% RH and ICH Q3D elemental impurity limits apply to the finished granules. The terminal finished product is an oral granule in a single-dose sachet intended for suspension or direct administration, and the process boundary is avoidance of aqueous granulation because the acetate esters undergo measurable hydrolysis under aqueous pH conditions above pH 6.0 at elevated temperature.
Injectable use of the tetraacetate is not supported by a marketed product; published formulation data for this specific protected acetate configuration is limited, but the absence of free hydroxyls reduces aqueous solubility below that of the parent aglycone and necessitates a lyophilized dosage form if sterile administration is required. A typical development formulation uses a 10 mL glass vial filled with 2 mL of a 5.0 mg/mL tetraacetate solution, corresponding to 10 mg tetraacetate per vial or 7.3 mg parent-equivalent, with bulking agents mannitol 25 mg/mL and sucrose 10 mg/mL. The solution is prepared in Water for Injection containing 30% (v/v) tert-butanol to solubilize the acetate during aseptic filtration through a 0.22 μm PVDF membrane, then lyophilized in a freeze dryer with a shelf ramp of 1.0 °C/min to -40 °C, primary drying at -25 °C and 100 μbar for 24 h, and secondary drying at +25 °C for 6 h. Cake moisture is controlled to ≤1.0% by Karl Fischer. The sterility assurance boundary is anchored to USP <1>, USP <71>, Ph.Eur. 2.6.1, and ISO 13408-1; residual solvent limits follow ICH Q3C. The terminal finished product is a lyophilized cake for reconstitution before intravenous or subcutaneous use, with oxygen headspace ≤2.0% v/v to limit ester peroxidation.
| Lyo phase | Setpoint |
|---|---|
| Freezing ramp | 1.0 °C/min to -40 °C |
| Primary drying shelf | -25 °C |
| Chamber pressure | 100 μbar |
| Primary drying time | 24 h |
| Secondary drying | +25 °C for 6 h |
| End moisture | ≤1.0% |
The primary commercial downstream conversion of the tetraacetate is base-catalyzed deprotection to the empagliflozin base, a sodium-glucose cotransporter 2 inhibitor. In a glass-lined reactor equipped with pitched-blade turbine at 200 rpm, the substrate is dissolved at 0.20 M in anhydrous 4:1 THF/methanol and cooled to 0–5 °C before sodium methoxide 0.05 eq (5 mol%) is added over 20 min; the reaction is held at 0–5 °C for 1.5 h to complete acetyl removal while minimizing anomerization at the anomeric C-1 position of the tetrahydropyran ring. The quench is performed with acetic acid until pH 6.8–7.2, followed by addition of 8 volumes of purified water to precipitate the parent base, which is isolated by vacuum filtration on a 2.0 μm PTFE cloth and vacuum tray-dried at 45 °C for 12 h to a loss on drying ≤0.5%. Batch-to-batch yield under these controls is 85–92%, and residual methanol and methyl acetate are monitored against ICH Q3C limits; the conversion is governed by ICH Q7 for active pharmaceutical ingredients and the parent API is released by Ph.Eur. 2.2.29 liquid chromatography and USP <621>. The terminal finished product is empagliflozin base API (CAS 864070-44-0) suitable for downstream oral solid dosage manufacturing.
Serving as a process-related impurity marker in SGLT2 inhibitor analytical release, the tetraacetate finds a narrower but essential downstream use in reversed-phase HPLC system suitability training sets. When spiked into parent API at 0.05%, 0.10%, and 0.15% area, the acetate derivative elutes with a higher retention factor than the free hydroxylated aglycone under acetonitrile/0.1% trifluoroacetic acid gradient conditions, allowing resolution from the main peak to be qualified according to ICH Q2(R1). The reference material is prepared by preparative HPLC on a 250 × 4.6 mm, 5 μm C18 column, collected as a fraction, lyophilized, and dried at 40 °C for 8 h; purity acceptance is ≥98.0% by area normalization, with residual solvent compliance under ICH Q3C and ISO 17025 for reference material services. Addition of the standard at 1.0 mg/mL in methanol as a stock solution and dilution to 0.1 mg/mL for working standards aligns with USP <621> system suitability injections. The terminal finished product is a sealed amber reference standard vial, and the operational boundary is storage at 2–8 °C with desiccant to prevent acetyl hydrolysis and moisture uptake.
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Compound (2R,3R,4R,5S,6S)-2-(acetoxymethyl)-6-[4-chloro-3-(4-ethoxybenzyl)phenyl]tetrahydro-2H-pyran-3,4,5-triyl triacetate is the per-O-acetylated C-aryl glucoside commonly referenced as dapagliflozin tetraacetate. The CAS registry number 461432-25-7 identifies the defined stereoisomer; the molecular formula is C29H33ClO10 and the molecular weight is 577.03 g mol⁻¹. The four acetyl groups mask the secondary and primary alcohols of the free C-aryl glucoside, yielding a non-ionizable, lipophilic crystalline solid. The substance is handled as a pharma-grade advanced intermediate under ICH Q7 and Q11 cGMP controls. It is not a compendial active pharmaceutical ingredient with an official USP or Ph. Eur. monograph; specification limits are therefore supplier and contract defined.
The stereochemical descriptors (2R,3R,4R,5S,6S) correspond to the D-gluco C-aryl series after numbering the tetrahydropyran ring with oxygen as position 1. The aryl group is attached at the anomeric carbon through a C–C bond. This C-aryl linkage is chemically distinct from O-glycosidic linkages in conventional glucosides and is not cleaved by ordinary glycoside hydrolases. The acetyl esters, however, are hydrolytically labile under alkaline conditions and are removed to generate the active SGLT2 inhibitor dapagliflozin. The theoretical free-base equivalent of the tetraacetate is 70.86% w/w, based on the molecular weight of dapagliflozin base 408.88 g mol⁻¹.
Direct blending of the tetraacetate into tablet, capsule, granule, or injectable matrices is not supported by public finished-dose monographs. The substance is practically insoluble in water, and its four acetate esters introduce hydrolytic instability in aqueous vehicles and wet granulation processes. Moisture ingress above 0.5% w/w is capable of liberating acetic acid, shifting related-substance profiles and lowering assay. The free C-aryl glucoside dapagliflozin, not the tetraacetate, is the active moiety; therefore weight-for-weight substitution into an oral dosage form would require a correction factor and would still require in vivo equivalence data unless the protected form were deliberately developed as a prodrug. Published data for the tetraacetate as a finished-dose prodrug is limited.
The tetraacetate is used primarily as a protected intermediate in the synthesis of dapagliflozin. The protecting groups improve crystallinity and simplify purification, but they also require quantitative removal before salt formation and final formulation. In a typical downstream step, the tetraacetate is treated with catalytic sodium methoxide in methanol at ambient temperature under nitrogen. The pH is maintained above 10 until HPLC shows disappearance of the starting tetraacetate. The mixture is then neutralized with acetic acid or an acidic ion-exchange resin, extracted into ethyl acetate, and crystallized as dapagliflozin base or converted to dapagliflozin propanediol monohydrate.
Release specifications for this protected intermediate are not published by pharmacopoeias. A representative cGMP release package includes identity, assay, related substances, residual solvents, water, residue on ignition, and elemental impurities. Analytical methods are generally validated according to ICH Q2(R2). HPLC area normalization is used for assay and impurity control because the aryl chromophore gives reliable UV response. The table below summarizes representative controls used in industrial supplier agreements for dapagliflozin tetraacetate.
| Parameter | Representative control | Reference method |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual inspection |
| Identification | HPLC retention time consistent with reference standard | HPLC-UV |
| Assay | ≥98.0% area | HPLC area normalization |
| Largest unspecified impurity | ≤0.10% | HPLC area normalization |
| Total impurities | ≤1.0% | HPLC area normalization |
| Water | ≤0.50% w/w | Karl Fischer, USP <921> |
| Residue on ignition | ≤0.10% w/w | USP <281> |
| Residual solvents | Class 1 and Class 2 limits | GC-HS, ICH Q3C |
| Elemental impurities | Route-dependent limits | ICP-MS, ICH Q3D |
The acceptance criteria above are representative of cGMP release for an advanced synthetic intermediate; they are not a formal regulatory specification. Because no public pharmacopoeial monograph exists, exact limits can vary by manufacturer and by the synthetic route used. The impurity profile is route-dependent and should be reviewed for deacetylated homologues, positional isomers, and residual metal catalysts.
Residual solvent control follows ICH Q3C. Methanol, ethyl acetate, dichloromethane, and tetrahydrofuran are common process solvents in the acetylation and purification sequence. The ICH Q3C Class 2 limits for methanol, ethyl acetate, dichloromethane, and tetrahydrofuran are 3000 ppm, 5000 ppm, 600 ppm, and 720 ppm, respectively. Class 1 solvents such as benzene must be absent or controlled below 2 ppm unless a route-specific justification is provided.
Elemental impurities are assessed against ICH Q3D using the intended deprotection and salt conversion sequences. Palladium is relevant when a palladium-catalyzed coupling or hydrogenation step is used in the synthesis of the C-aryl glucoside. A route-dependent palladium limit of ≤10 ppm is commonly applied because the metal can persist through crystallization and interfere with the final dapagliflozin propanediol monohydrate specification. Cadmium, lead, arsenic, and mercury are controlled as Class 1 elemental impurities. Because the tetraacetate is not an injectable final product, the Q3D parenteral risk assessment is not applied until the deprotected form is converted to a parenteral-grade salt if such a formulation is developed.
For injectable use, the tetraacetate itself is not suitable without hydrolysis and salt selection. After deprotection, residual methanol and methylene chloride must meet ICH Q3C limits, and the final injectable grade would require additional control of endotoxins, bioburden, and particulate matter according to Ph. Eur. 2.6.14 or USP <85>. No approved parenteral dapagliflozin finished product is described in major pharmacopoeias; published data for this specific configuration as an injectable API is limited.
The difference between the tetraacetate and the final active is not merely molecular weight. The tetraacetate is neutral, crystalline, and organic-solvent soluble; dapagliflozin base is a polar C-aryl glucoside with poor aqueous solubility and a high hydrogen-bonding capacity. For oral solid dosage forms, the free base is typically isolated as dapagliflozin propanediol monohydrate, CAS 960404-59-5, with molecular weight 502.98 g mol⁻¹. This salt form provides better crystallinity and handling than the free base. The approved oral tablets contain 5 mg or 10 mg of dapagliflozin as the propanediol monohydrate.
Process conversion from the tetraacetate to dapagliflozin propanediol monohydrate requires strict control of the deacetylation endpoint. Incomplete deprotection leaves acetylated impurities that may cocrystallize with the final salt. Over-exposure to base can generate oxidized impurities at the benzylic methylene position. The reaction is therefore monitored by HPLC at an early time point and at endpoint, with intermediate sampling to confirm the disappearance of mono-, di-, and triacetyl intermediates. The anomeric C–C bond is stable under the alkaline deprotection conditions; the principal side reactions are ester hydrolysis and oxidation rather than anomerization or C–glycosidic cleavage.
After deprotection and salt formation, the final dapagliflozin API can be processed by direct compression or wet granulation for tablets. Granule-based oral dosage forms require particle-size control of the active after milling; laser diffraction according to USP <429> or ISO 13320 is commonly used to monitor d10, d50, and d90. Capsule and granule formulations may be developed from the same milled API, but the tetraacetate is not used directly in these operations because it would require a stoichiometric correction for the free-base equivalent and because the acetyl groups would introduce a different dissolution and stability profile.
For injectable development, the deprotected API would require salt selection, aqueous solubility assessment, pH stability profiling, and terminal sterilization or aseptic processing. No public injectable monograph or approved injectable formulation for dapagliflozin exists; therefore any injectable application of the tetraacetate-derived material would require full pharmaceutical development, including compatibility with parenteral excipients, container closure systems, and endotoxin control. The tetraacetate is not interchangeable with the propanediol monohydrate salt on a weight basis, and the two materials have different residual solvent, moisture, and impurity risk profiles.
Storage of the tetraacetate is normally conducted in sealed, moisture-resistant containers under nitrogen at controlled room temperature or 2–8 °C, depending on the manufacturer’s stability data. The material should not be exposed to open atmospheric moisture for extended periods, because acetyl hydrolysis can occur at the powder surface. When the compound is transferred to production, containers should be warmed to ambient temperature before opening to avoid condensation. These handling controls are particularly important when the tetraacetate is intended for conversion to a final active rather than for direct formulation, because residual moisture and free acetic acid can affect downstream pH adjustment and crystallization behavior.