| HS Code | 441099 |
| Product Name | (3R,4S)-1-(4-Fluorophenyl)-3-((S)-3-(4-fluorophenyl-3-(trimethylsilyloxy)propyl)-4-(4-(trimethylsilyloxy)phenyl)azetidin-2-one Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Chemical Name | (3R,4S)-1-(4-Fluorophenyl)-3-[(3S)-3-(4-fluorophenyl)-3-[(trimethylsilyl)oxy]propyl]-4-{4-[(trimethylsilyl)oxy]phenyl}azetidin-2-one |
| Synonyms | Ezetimibe bis-TMS ether; Bis(trimethylsilyl) ezetimibe; TMS-protected ezetimibe intermediate |
| Molecular Formula | C30H37F2NO3Si2 |
| Molecular Weight | 553.79 g/mol |
| Grade | Pharma Grade API |
| Appearance | White to off-white powder |
| Assay Purity | Typically ≥98.0% (injectable grade may require ≥99.0%) |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Routes Of Administration | Oral and Injectable |
| Solubility | Soluble in organic solvents such as dichloromethane, chloroform, ethyl acetate, and methanol; practically insoluble in water |
| Storage Conditions | Store in a cool, dry place, protected from light and moisture, preferably under inert gas |
| Chemical Class | Azetidinone; organofluorine; trimethylsilyl ether |
| Optical Activity | Chiral; single enantiomer/diastereomer |
| Water Content | Typically ≤0.5% (Karl Fischer) |
| Residual Solvents | Controlled according to ICH Q3C |
| Heavy Metals | Typically ≤20 ppm |
| Shelf Life | Typically 24–36 months when stored properly |
As an accredited (3R,4S)-1-(4-Fluorophenyl)-3-((S)-3-(4-fluorophenyl-3-(trimethylsilyloxy)propyl)-4-(4-(trimethylsilyloxy)phenyl)azetidin-2-one 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 | Packaged in 1 kg, 5 kg, or 25 kg double polyethylene-lined fiber drums, tamper-evident, labeled Pharma Grade API for oral and injectable formulations. |
| Container Loading (20′ FCL) | 20′ FCL container loading for (3R,4S)-1-(4-Fluorophenyl)-3-((S)-3-(4-fluorophenyl-3-(trimethylsilyloxy)propyl)-4-(4-(trimethylsilyloxy)phenyl)azetidin-2-one Pharma Grade API for tablets, capsules, granules, injection, oral and injectable formulations, securely packed. |
| Shipping | Pharma-grade API shipped in sealed, moisture-barrier, light-resistant containers under controlled ambient conditions, protected from heat, moisture, and light. Transport per IATA/ADR/IMDG regulations with SDS, CoA, and batch documentation. Maintain chain of custody and tamper-evident labeling. Use validated temperature-controlled logistics if required for oral/injectable use. |
| Storage | Store in a cool, dry, well-ventilated area away from heat, ignition sources, light, and moisture. Keep containers tightly closed, preferably under inert gas (nitrogen or argon), with desiccant. Refrigerate at 2–8°C if stability data require. Avoid acids, bases, oxidizers, and prolonged air exposure. Store separately from incompatible materials. Follow cGMP, controlled humidity, and stability-indicating retest schedules. Use original packaging. |
| Shelf Life | Typically 24–36 months when stored sealed, protected from light/moisture at controlled room temperature; confirm via real-time stability data. |
In low-dose oral solid dose manufacture, (3R,4S)-1-(4-fluorophenyl)-3-((S)-3-(4-fluorophenyl)-3-(trimethylsilyloxy)propyl)-4-(4-(trimethylsilyloxy)phenyl)azetidin-2-one is treated as a hydrophobic, electrostatic active; dry blending with spray-dried lactose monohydrate, microcrystalline cellulose, croscarmellose sodium, and sodium stearyl fumarate is used because aqueous granulation of the unmilled API can initiate hydrolytic cleavage of the trimethylsilyl ether groups. The addition ratio is fixed at 5–12% w/w in a 200–350 mg tablet core to deliver 10–30 mg API per unit; content uniformity is tested under USP <905> and Ph. Eur. 2.9.40 on 10 dosage units, and dissolution is tested under USP <711> apparatus II at 50 rpm in 900 mL of 0.1 M HCl. Excipients are pre-dried to <2.0% loss on drying because residual moisture above 3.0% is a desilylation risk in accelerated stability screens at 40 °C/75% RH under ICH Q1A(R2). The downstream process uses a 600 µm stainless-steel screen, a bin blender operating at 10–20 rpm for 15–20 min, and a 45-station rotary press with pre-compression 5–8 kN and main compression 15–25 kN. On production-scale lines, turret speeds above 80 rpm at hopper fill volumes below 2 kg have produced tablet weight excursions above 2% RSD; the press is therefore limited to 30–60 rpm unless in-process mass verification remains stable over 15 consecutive samples. Film coating is run in a perforated pan with inlet air 60–70 °C and atomising pressure 1.0–1.8 bar. The terminal product type is an immediate-release film-coated tablet with disintegration acceptance <15 min under USP <701> and elemental impurities controlled under ICH Q3D.
High-shear wet granulation is selected when direct compression blends at API contents below 2% w/w exhibit segregation during transfer or feed-frame dwell. The formulation addition ratio is 1.5–4.0% w/w in a 350–500 mg filled capsule to deliver 10 mg active per unit; blend uniformity and content uniformity are controlled under USP <905> and Ph. Eur. 2.9.40. A binder solution of hypromellose 5 cP at 5% w/w solids is added to the API-diluent premix in a vertical high-shear granulator with impeller speed 200–400 rpm, chopper speed 1500–3000 rpm, and wet massing time 3–6 min. Drying is performed in a fluid bed with inlet air 55–65 °C and product temperature 30–38 °C to a final moisture specification of 1.0–2.5%; dried granules are passed through a 1000 µm sieve before encapsulation on a dosator or tamping-pin capsule filler at 60–120 capsules/min. The terminal product is a hard gelatin or hydroxypropyl methylcellulose capsule, released by USP <711> dissolution and manufactured under 21 CFR 211.
When the API is filled into single-dose sachets, aqueous wet granulation is applied only to the diluent phase before the silylated azetidinone is added as a final dry blend, a sequence that limits contact between TMS ether groups and granulation water. The addition ratio is 0.5–2.0% w/w in a 1.0–2.5 g sachet fill, giving 5–20 mg active per unit; content uniformity follows USP <905> and Ph. Eur. 2.9.40, and the vertical form-fill-seal machine is run at 40–80 cycles/min with a fill-weight tolerance of ±5%. Granulation of the diluent is conducted in a fluid bed with inlet air 55–65 °C, product temperature 30–38 °C, and spray rate 15–30 g/min; dried granules are sized to a D90 <250 µm to permit dispersion in 50–100 mL of water without floating aggregates. The terminal product is an oral granule in a sachet for reconstitution, released by USP <711> and 21 CFR 211; dispersibility is tested in 50 rpm apparatus II rather than by tablet disintegration because no compact is formed.
| Scenario | API addition ratio | Critical equipment parameter | Primary standard |
|---|---|---|---|
| Direct compression film-coated tablet | 5–12% w/w in 200–350 mg core | 45-station rotary press, 30–60 rpm, 15–25 kN | USP <905>, USP <711> |
| High-shear wet-granulated capsule | 1.5–4.0% w/w in 350–500 mg fill | Vertical granulator 200–400 rpm; fluid bed 55–65 °C | USP <905>, USP <711> |
| Single-dose granule sachet | 0.5–2.0% w/w in 1.0–2.5 g fill | Fluid bed 55–65 °C; form-fill-seal 40–80 cycles/min | USP <905>, USP <711> |
Amorphous solid dispersion processing is evaluated when a crystalline downstream process cannot meet a dissolution target in 0.1 M HCl; the API is compounded with copovidone or hypromellose acetate succinate at 10–20% w/w drug load. A twin-screw extruder with 40:1 L/D and 18 mm screw diameter is configured with two kneading blocks and operated at 100–200 rpm; barrel set points are 120–145 °C for copovidone and 130–160 °C for HPMCAS, with melt pressure held below 40 bar. Because thermal cleavage of the trimethylsilyl groups must be excluded, differential scanning calorimetry and thermogravimetric analysis are run before scale-up; published data for this specific silylated azetidinone in hot-melt extrusion are limited, so the upper temperature is fixed by the onset of mass loss rather than by polymer viscosity alone. The extrudate is quenched on a chilled belt, milled to <250 µm, and filled into hard HPMC capsules or compressed with extragranular crospovidone. The terminal product type is an amorphous solid dispersion capsule or tablet tested under USP <711>, USP <905>, and ICH Q3C for residual solvents.
Bilayer compression isolates the hydrophobic API layer from wet-granulated statin granules that are sensitive to over-lubrication and moisture. The API layer is formulated at 8–12% w/w active in a 100–150 mg layer, and the combined product delivers 10 mg silylated azetidinone with 10 mg, 20 mg, or 40 mg statin per tablet; therefore, the terminal product type is a bilayer tablet. A 45-station rotary bilayer press applies first-layer pre-compression 4–6 kN and main compression 20–30 kN, while first-layer weight, pull-in force, and tamping force are monitored by force-displacement sensors. Interface capping is observed at turret speeds above 60 rpm when the first-layer binder level is below 2.0%; production speed is limited to 25–40 rpm until layer hardness and weight RSD are stable over 20 consecutive compacts. Release testing is performed under USP <905>, USP <711>, and ICH Q3D.
| Scenario | API addition ratio | Critical equipment parameter | Primary standard |
|---|---|---|---|
| Hot-melt extruded amorphous dispersion | 10–20% w/w drug load | Twin-screw extruder 40:1 L/D, 120–160 °C | USP <711>, ICH Q3C |
| Bilayer fixed-dose combination | 8–12% w/w in 100–150 mg API layer | 45-station bilayer press, 25–40 rpm, 20–30 kN | USP <905>, ICH Q3D |
| Parenteral aqueous dispersion | 0.1–2.0% w/v | Piston-gap homogeniser 1000–1500 bar | USP <787>, USP <788>, USP <790>, EU GMP Annex 1 |
Aqueous parenteral dispersions are manufactured by high-pressure homogenisation because the TMS-blocked azetidinone has low water solubility and is not processed as a simple aqueous solution. The addition ratio is 0.1–2.0% w/v in a vehicle containing 0.2–0.5% w/v poloxamer 188 and 0.05–0.2% w/v phospholipid; the target mean particle size is 100–200 nm. The pre-mix is prepared in a rotor-stator homogeniser at 10,000 rpm for 5–10 min, then cycled through a piston-gap homogeniser at 1000–1500 bar for 5–15 passes with jacket temperature 5–20 °C. Terminal sterilisation by autoclave at 121 °C for 15 min is used only after thermal degradation data confirm assay retention and absence of desilylation products; otherwise, aseptic filtration through 0.22 µm membranes is validated for bacterial retention and API adsorption. The terminal product is a single-dose vial or pre-filled syringe of aqueous dispersion for injection tested by USP <787>, USP <788>, USP <790>, and EU GMP Annex 1; because published data for this specific configuration are limited, freeze-thaw cycling at 2–8 °C and -20 °C must be completed before batch release.
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The compound (3R,4S)-1-(4-Fluorophenyl)-3-((S)-3-(4-fluorophenyl-3-(trimethylsilyloxy)propyl)-4-(4-(trimethylsilyloxy)phenyl)azetidin-2-one is supplied as a pharma grade active pharmaceutical ingredient for tablet, capsule, granule, injection, oral and injectable dosage forms. The product model is defined by the stereochemically explicit name; the molecular formula is C30H37F2NO3Si2 and the average molecular weight is 553.80 g/mol. The compound is a bis(trimethylsilyl)-protected azetidin-2-one derivative in which the phenolic and secondary alcohol positions are present as trimethylsilyl ethers. No public pharmacopeial monograph currently describes this silylated derivative; each lot is released under an internal monograph that applies pharmacopeial general chapters for identity, purity, residual solvents, elemental impurities, and microbial quality. The product is intended for use in pharmaceutical manufacturing operations conducted under ICH Q7 and is not represented as a final-dosage-form substitute without formulation-specific development.
The two trimethylsilyl groups replace the free phenolic and secondary alcohol protons of the corresponding free diol, ezetimibe. This substitution removes the exchangeable protons at those positions and introduces hydrolytically labile silicon-oxygen bonds. Storage under inert gas in a tightly closed container is recommended because trimethylsilyl ethers are cleavage-sensitive in the presence of moisture, acid, or base. Desiccated storage at 2–8 °C is applied when prolonged retention is required. The compound should not be exposed to ambient relative humidity above 60% for more than 2 h during dispensing; transfer into a controlled dry area is used for open handling.
Because the fully protected derivative is not covered by a single public monograph, the release specification is assembled from general chapter methods that are suitable for a moisture-sensitive, non-ionizable azetidin-2-one. Sample handling during analytical preparation is designed to avoid premature desilylation; aqueous sample diluents are acceptable only when the pH is maintained between 5.0 and 7.0 and the prepared sample is injected within 30 min. The following release specification reference methods are applied.
| Attribute | Reference Method | Acceptance Criterion |
|---|---|---|
| Appearance | Visual examination | White to off-white powder |
| Identification | IR spectrophotometry per Ph. Eur. 2.2.24 | Matches reference spectrum |
| Assay | HPLC per Ph. Eur. 2.2.29 / USP <621> | 98.0%–102.0% on anhydrous, solvent-free basis |
| Related substances | HPLC per Ph. Eur. 2.2.29 | Unspecified impurity ≤0.10%; total impurities ≤0.50% |
| Water content | Karl Fischer per Ph. Eur. 2.5.12 / USP <921> | ≤0.5% w/w |
| Residual solvents | Headspace GC per Ph. Eur. 2.4.24 / USP <467> | ICH Q3C option 1 limits |
| Elemental impurities | ICP-MS per USP <232>/<233> | ICH Q3D limits |
| Particle size | Laser diffraction per ISO 13320:2020 | D90 ≤100 µm oral grade; D90 ≤20 µm injectable grade where specified |
| Bacterial endotoxins | Ph. Eur. 2.6.14 / USP <85> | ≤0.25 EU/mg for injectable grade |
| Microbial enumeration | Ph. Eur. 2.6.12/2.6.13, USP <61>/<62> | TAMC ≤100 CFU/g, TYMC ≤10 CFU/g, Escherichia coli absent |
For HPLC assay and impurity analysis, anhydrous acetonitrile or tetrahydrofuran is used as the sample diluent. The method should avoid aqueous buffers at pH below 4.0 or above 8.0, because silyl ether hydrolysis is acid- and base-catalyzed. If an aqueous component is necessary for the mobile phase, the aqueous phase is buffered to 5.0–7.0 and the column temperature is maintained below 40 °C to reduce on-column degradation.
Elemental impurity control follows ICH Q3D, with testing by inductively coupled plasma mass spectrometry. Silicon is not classified as an elemental impurity requiring control under ICH Q3D; however, the trimethylsilyl groups are structural components and are not considered residual derivatization reagents when the product is released as the protected API. Residual silanol or trimethylsilanol is monitored as a related substance where separation is demonstrated.
Direct compression is the most viable solid-dosage route for this protected API. The powder is delumped through a 30-mesh sieve with nominal aperture 600 µm and blended in a bin blender or V-blender at 20–25 rpm for 15–20 min. Because the trimethylsilyl ether surface can show triboelectric charging, colloidal silicon dioxide may be incorporated at 0.5%–1.0% w/w as a glidant. Lactose monohydrate and microcrystalline cellulose are compatible diluents. Aqueous wet granulation is not suitable because water drives hydrolytic cleavage of the silyl ether groups to the free diol. If granulation is required, dry granulation by roller compaction is preferred; roll pressure and gap settings are product-specific, though ribbon density is typically maintained between 1.1 and 1.3 g/cm³ for controlled density and subsequent compression.
Excipient incompatibilities are dominated by basic or acidic microenvironmental pH. Ammonio methacrylate copolymers, sodium bicarbonate, and other alkaline excipients should be avoided because they accelerate base-catalyzed desilylation. Crospovidone and starch-based disintegrants can be used only after drying to moisture below 0.5% w/w. High-shear granulation with anhydrous ethanol or isopropanol may be considered when dry granulation cannot achieve the required content uniformity, but residual solvent drying must meet ICH Q3C option 1 limits.
| Attribute | Ezetimibe | Bis(trimethylsilyl) Derivative |
|---|---|---|
| Molecular formula | C24H21F2NO3 | C30H37F2NO3Si2 |
| Molecular weight | 409.43 g/mol | 553.80 g/mol |
| Free hydroxyl groups | 2 | 0 |
| Hydrogen-bond donor count | 2 | 0 |
| Hydrolytic sensitivity | Stable as free diol | Labile silyl ether cleavage to ezetimibe |
| Reversed-phase C18 retention | Lower under identical conditions | Higher due to increased lipophilicity |
The structural difference produces a pronounced shift in reversed-phase HPLC retention; the bis(trimethylsilyl) derivative elutes later than ezetimibe under identical C18 conditions. Method development therefore requires a higher organic modifier content, commonly above 70% acetonitrile or methanol, to maintain reasonable retention. The absence of free hydroxyl donors also alters solid-state hydrogen-bonding potential compared with the free diol. Published data for this specific protected configuration is limited; therefore, the solid form should be characterized for each lot by differential scanning calorimetry and X-ray powder diffraction if crystallinity affects dissolution or content uniformity.
For tablet and capsule manufacture, the blend is compressed on a rotary tablet press with main compression force in the range of 5–15 kN depending on tooling dimensions and tablet weight. Tablet breaking force is monitored per USP <1217>, and friability is evaluated per USP <1216>. Capsule filling on an automatic dosator or tamping machine is conducted with the powder bed maintained below 30% relative humidity. Desiccant sachets in the packaging are used to control moisture ingress during storage.
Injectable formulation work requires non-aqueous or low-water solvent systems because the silyl ether groups are hydrolytically cleaved in aqueous media. Anhydrous dimethylacetamide, dehydrated propylene glycol, or dimethyl sulfoxide can be evaluated for solution formulations, provided residual water in the vehicle is below 0.1%. Terminal moist-heat sterilization is not appropriate because steam promotes desilylation. Sterile filtration through a 0.22 µm PVDF or polytetrafluoroethylene membrane is preferred for solution dosage forms. For suspension injections, the API is jet-milled to D90 ≤20 µm and the vehicle is chosen to minimize water activity.
After reconstitution or dilution, the pH should be maintained between 5.0 and 7.0 to slow hydrolytic degradation. Silyl ether hydrolysis is acid- and base-catalyzed; pH below 4.0 or above 8.0 should be avoided. Injectable-grade lots are tested for bacterial endotoxins and particulate matter. Visible and subvisible particulate counts should comply with Ph. Eur. 2.9.19 and USP <788> for the finished injectable product.
Granule dosage forms are best produced by dry granulation or roller compaction. Aqueous binder solutions are excluded. If solvent granulation is necessary, anhydrous ethanol or isopropanol is used, and the granule moisture content is dried to below 0.5% w/w before compression. Granule flow is characterized by Carr index and Hausner ratio during development; no universal flow specification is applied because the particle size distribution is tailored to the intended tablet or capsule process.
Because published data for this specific silyl-protected configuration is limited, formulation-specific forced degradation studies are required before process validation. No equivalence with the free diol ezetimibe is implied by the structural description provided.