| HS Code | 275818 |
| Api Name | Fezolinetant |
| Synonyms | E2027 |
| Cas Number | 1629229-37-5 |
| Grade | Pharma Grade |
| Product Form | Active Pharmaceutical Ingredient Powder |
| Appearance | White to off-white crystalline powder |
| Purity | ≥99.0% by HPLC |
| Drug Class | Neurokinin-3 (NK3) receptor antagonist |
| Molecular Target | TACR3 / NK3 receptor |
| Mechanism Of Action | Selectively blocks neurokinin B signaling at hypothalamic KNDy neurons to modulate thermoregulation |
| Primary Indication | Moderate to severe vasomotor symptoms associated with menopause |
| Dosage Form Compatibility | Tablet, capsule, granule, and injection |
| Route Compatibility | Oral and injectable |
| Solubility Profile | Soluble in suitable organic solvents; injectable formulations require appropriate solubilizing vehicle systems |
| Moisture Sensitivity | Protect from excessive moisture |
| Storage Condition | Store tightly sealed in a dry, cool, well-ventilated area; protect from light |
| Stability Statement | Stable under normal pharmaceutical storage and handling conditions |
As an accredited Fezolinetant 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 sealed double-layer polyethylene bags inside aluminum foil pouches, then placed in fiber drums. Net weight: 25 kg per drum. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Fezolinetant Pharma Grade API, suitable for tablet, capsule, granule, oral, and injectable formulations. |
| Shipping | Fezolinetant Pharma Grade API ships in sealed, inert, light-protected containers under temperature-controlled conditions to preserve stability. Documentation includes Certificate of Analysis and MSDS. Handling follows GMP guidelines. Export packaging ensures safe transit for oral and injectable formulations, with cold-chain options available upon request. |
| Storage | Store Fezolinetant Pharma Grade API in a tightly sealed, light-resistant container in a cool, dry, well-ventilated area. Keep away from excessive heat, moisture, and incompatible materials. Maintain controlled room temperature, typically 20–25°C, with proper labeling. For oral and injectable dosage forms, ensure strict hygiene, avoid contamination, and follow all handling and safety guidelines. |
| Shelf Life | Fezolinetant API shelf life is typically 24 months under recommended storage conditions, ensuring stability for oral and injectable dosage forms. |
For commercial production of a 45 mg fezolinetant immediate-release tablet, direct compression is selected only after the API particle-size distribution, bulk density, and residual moisture content are confirmed to align with the site’s validated blending and compression parameters. The formulation addition proportion is calculated from the target tablet core mass rather than fixed by a universal percentage: a 250 mg core containing 45 mg fezolinetant corresponds to 18.0 wt%, a 200 mg core to 22.5 wt%, and a 300 mg core to 15.0 wt%. Industry compliance for this route is documented against 21 CFR 211.110 for in-process blend uniformity, weight variation, and sampling of the powder bed, 21 CFR 211.165 for finished-product release testing, ICH Q7 for control of raw materials and intermediates, USP <905> for uniformity of dosage units, USP <711> for dissolution, and USP <1216> for tablet friability. The downstream process typically includes co-sieving of fezolinetant with microcrystalline cellulose and lactose monohydrate, dry blending in a bin blender or V-blender, addition of croscarmellose sodium as a disintegrant, final lubrication with magnesium stearate, and compression on a rotary tablet press equipped with pre-compression and ejection-force monitoring. On production-scale equipment, the main failure modes that define the operating window are capping and lamination at low pre-compression force, weight drift from poor powder flow in the feed frame, and friability increase when the compression force falls below the formulation-specific threshold. The terminal finished product is a film-coated immediate-release tablet containing 45 mg fezolinetant per unit.
Selection of high-shear wet granulation is justified when direct compression fails to maintain content uniformity across the batch, when API dusting creates occupational exposure concerns, or when the powder blend cannot sustain high-speed tablet press operation without segregation. In this route, the 45 mg fezolinetant dose is granulated at the same dry-basis addition proportion as a direct-compression core; for a 250 mg final tablet core, fezolinetant remains 18.0 wt% of the dry granule matrix, with binder solids included in the extragranular calculation. Compliance is governed by 21 CFR 211.110 for granule blend uniformity and moisture testing, ICH Q7 for granulation endpoint and drying records, USP <905> for uniformity of dosage units, USP <711> for dissolution, and USP <1216> for tablet friability after compression. The downstream process uses a high-shear granulator with a main impeller and side chopper; fezolinetant, filler, and binder are dry-mixed, then wetted with an aqueous binder solution delivered at a fixed rate through a nozzle. Endpoint is controlled by impeller power consumption or torque rather than by granulation time alone, because overgranulation increases granule densification and can retard drug release under USP <711>. If the torque endpoint is missed, the granules may require reprocessing or batch rejection because milling cannot fully reverse the porosity loss. Wet granules are dried in a fluid-bed dryer or tray dryer, milled through a conical mill with a defined screen size, and blended with extragranular croscarmellose sodium and magnesium stearate before compression. The downstream dosage form after final blending and compression is a 45 mg immediate-release film-coated tablet; alternatively, the dried granule may be encapsulated if flow specifications are met.
Alternatively, roller compaction is evaluated when the 45 mg fezolinetant formulation must avoid aqueous granulation because of process train limitations or when a continuous dry-granulation route is selected for scale-up. The API addition proportion is derived from the same core-mass calculation; a 250 mg compressed core places fezolinetant at 18.0 wt%, with intragranular and extragranular disintegrant fractions assigned by the development protocol. Regulatory expectations are met through 21 CFR 210/211, ICH Q7, USP <905> for uniformity of dosage units, USP <711> for dissolution, and USP <1216> for tablet friability. The downstream process comprises blending fezolinetant with microcrystalline cellulose, lactose or mannitol, and a portion of croscarmellose sodium; compacting the blend in a roller compactor with controlled roll pressure, roll speed, and gap; milling the ribbons through an oscillating or conical mill; blending the granules with extragranular disintegrant and magnesium stearate; and compressing on a rotary tablet press. Roll pressure is a critical process parameter because excessive pressure reduces granule porosity and produces a property cliff-edge effect: disintegration time rises sharply once granule density exceeds the formulation-specific threshold, and dissolution failure may follow under USP <711>. Product-specific published data for fezolinetant roller compaction are limited; therefore, the operating window must be established through design of experiments using content uniformity, friability, and dissolution as acceptance criteria. The resulting dosage form is a 45 mg immediate-release film-coated tablet manufactured without an aqueous granulation step.
In capsule filling operations, the 45 mg fezolinetant dose is distributed into a two-piece hard capsule from a powder blend or granulated intermediate, and the addition proportion is set by the validated fill weight rather than by a fixed percentage. A 300 mg fill for a size 1 capsule yields 15.0 wt% fezolinetant, a 400 mg fill for a size 0 capsule yields 11.25 wt%, and a 250 mg fill yields 18.0 wt%, provided the fill mass is maintained within the acceptance limits of USP <905>. Compliance for encapsulated fezolinetant batches is assessed with 21 CFR 211.110 for in-process fill weight control, 21 CFR 211.165 for release testing, USP <905> for uniformity of dosage units, USP <711> for dissolution, and USP <701> for disintegration where required by the filing. The downstream process involves blending fezolinetant with lactose monohydrate, microcrystalline cellulose, and croscarmellose sodium; filling the blend on a tamping-pin or dosator capsule machine; regulating fill weight through tamping depth or dosator volume; and sealing the filled capsules. Environmental controls, typically 40–50% RH, are required because capsule shell moisture exchange can alter powder flow and shell brittleness, leading to weight variation or shell cracking on high-speed fillers. The terminal finished product is a hard gelatin or hypromellose capsule containing 45 mg fezolinetant for oral administration.
Fezolinetant is approved as an oral tablet, and no commercial injectable formulation is described in current public marketing authorizations; injectable development therefore remains in early feasibility screening, and published data for this specific configuration are limited. A fixed commercial addition proportion cannot be assigned without validated solubility, stability, and osmolality data. General screening of poorly water-soluble neutral APIs for injectable use commonly evaluates drug loads between 5 mg/mL and 20 mg/mL using pH adjustment, co-solvents, surfactants, or cyclodextrins, but these figures are not product-specific and must not be interpreted as a proven fezolinetant formula. Compliance for injectable manufacture is governed by 21 CFR 210/211, USP <1> for injections, USP <71> for sterility testing, USP <85> for bacterial endotoxins, USP <788> for particulate matter, and ICH Q3D for elemental impurities. The downstream process, if a solution formulation is feasible, would require dissolution of fezolinetant in a suitable vehicle, aseptic filtration through a validated sterilizing-grade membrane, and filling into depyrogenated vials or ampoules under ISO 14644 cleanroom conditions. If solubility is insufficient for a terminally sterilized solution, lyophilization may be evaluated; the process would include filling a bulk solution, freezing, primary drying, and secondary drying to produce a lyophilized cake for reconstitution. Terminal sterilization should not be assumed without thermal degradation data. The terminal finished product for this scenario is an investigational injectable solution or lyophilized powder for reconstitution, not an approved commercial product.
A fluid-bed granulation campaign may be executed when the manufacturing site requires a dried granule intermediate that can be split between tablet compression and capsule filling without changing the API addition ratio. On a dry basis, fezolinetant is maintained at 18.0 wt% in a batch intended for 250 mg tablet cores or equivalent proportional capsule fill masses. Compliance is documented under 21 CFR 211.110 for granule moisture and blend uniformity, ICH Q7 for fluid-bed drying records and equipment cleaning, USP <905> for uniformity of dosage units after downstream filling or compression, and USP <711> for dissolution of the resulting dosage form. The process uses a top-spray fluid-bed granulator with a defined inlet air temperature, spray rate, and atomization pressure; the powder bed is preheated, a binder solution is sprayed onto the fluidized powder, and the material is dried to a target loss-on-drying before screening through a conical mill. The main process failure mode is overwetting, which forms large agglomerates, reduces yield at the screen, and changes granule density enough to shift dissolution; therefore, spray rate and product temperature are monitored continuously rather than controlled by batch time alone. Product-specific published data for fezolinetant fluid-bed granulation are limited, so the operating window must be set experimentally against the approved content uniformity and dissolution specifications. The terminal product of this unit operation is a controlled granule batch for compression or capsule filling; the patient-ready finished product derived from the granule is a 45 mg fezolinetant tablet or capsule.
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Fezolinetant pharma-grade active pharmaceutical ingredient is supplied as a white to off-white crystalline powder with an anhydrous molecular weight of 436.48 g/mol, molecular formula C24H25FN4O3, and CAS registry number 1629229-37-3. The material is designated non-compendial; release testing is therefore aligned with ICH Q6A, ICH Q7, and ICH Q11 rather than a specific United States Pharmacopeia or European Pharmacopoeia monograph. The approved oral reference product contains fezolinetant 45 mg administered once daily for moderate-to-severe vasomotor symptoms associated with menopause. The molecule acts as a selective neurokinin 3 receptor antagonist on hypothalamic KNDy neurons, reducing neurokinin B-mediated thermoregulatory dysregulation without direct activation of estrogen receptors. Representative API grades include FZNT-01-G for wet or dry granulation, FZNT-02-D for direct compression, and FZNT-03-I for injectable formulation development. Each grade is manufactured under ICH Q7, with analytical control supported by ICH Q2(R1) validation and impurity management according to ICH Q3A, ICH Q3C, ICH Q3D, and ICH M7. The API is not intrinsically sterile, and the oral solid dosage forms are manufactured under current good manufacturing practice governed by 21 CFR Part 210 and 21 CFR Part 211 after the API has been qualified under the appropriate active pharmaceutical ingredient GMP framework.
Because no compendial monograph is published for fezolinetant, the release file should contain a impurity control strategy justified under ICH Q11 Section 3.2 and a quality risk management description aligned with ICH Q9. The solid-state form is controlled by X-ray powder diffractometry because the approved oral tablet is a crystalline material. The main analytical burden is therefore the demonstration of identity, crystalline phase consistency, related substances, residual solvents, elemental impurities, water content, and particle size distribution. The absence of a monograph does not remove the requirement for a stability-indicating high-performance liquid chromatography method; the method is validated for specificity, linearity, accuracy, and precision according to ICH Q2(R1). Nitrosamine risk assessment is performed in alignment with ICH M7 and regional health authority guidance, with absence of N-nitrosodimethylamine confirmed at a limit derived from the acceptable intake established in the relevant regulatory assessment.
Identity confirmation for release includes infrared spectral matching against a qualified reference standard, X-ray powder diffractogram matching against the designated crystalline pattern, and chromatographic retention time consistency with the reference standard. Differential scanning calorimetry and thermogravimetric analysis are used to support solid-state characterization, while residual solvent analysis is performed by headspace gas chromatography. The release specification is established from manufacturing process validation and stability data under ICH Q1A(R2). The specification below is a representative release panel for oral-grade fezolinetant API; injectable-grade material may require additional bioburden and bacterial endotoxin controls.
| Parameter | Representative acceptance criterion | Analytical basis |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual inspection |
| Identification | Infrared spectrum matches reference; XRPD diffractogram matches crystalline pattern; HPLC retention time matches standard | USP <197>, USP <941>, ICH Q2(R1) |
| Assay by HPLC | 98.0–102.0% on dried, solvent-free basis | ICH Q2(R1) |
| Related substances | Unspecified impurity ≤0.10%; total impurities ≤0.5%; reporting threshold 0.05% | ICH Q3A |
| Water content | ≤0.5% w/w | Karl Fischer, USP <921> |
| Residue on ignition | ≤0.1% | USP <281> |
| Elemental impurities | Oral daily dose limits per ICH Q3D; parenteral limits where applicable | ICH Q3D |
| Residual solvents | Class 1 solvents not detected; Class 2 and Class 3 solvents within ICH Q3C limits | ICH Q3C, USP <467> |
| Microbiological quality, non-sterile oral grade | TAMC ≤100 CFU/g; TYMC ≤10 CFU/g; Escherichia coli absent | USP <61>, USP <62> |
The XRPD diffractogram should be evaluated for crystalline phase consistency because changes in polymorphic form can alter dissolution behavior in tablet and capsule formulations. If micronization is used, an amorphous content limit should be established and verified by a method that is validated for the expected amorphous fraction. Water content is not a surrogate for hydrate formation; a separate polymorph stability assessment under ICH Q1A(R2) conditions is required to establish the retest period. Residual solvent release depends on the synthetic route, and the solvent panel should include both process solvents and any solvents introduced during purification or recrystallization. Elemental impurity control follows the ICH Q3D risk assessment for the actual synthetic route, with particular attention to palladium or other transition metal catalysts if used in coupling steps.
Particle size distribution, bulk density, and flowability are adjusted for each dosage form. FZNT-01-G for granulation is lot-controlled to laser diffraction D90 ≤80 µm and D50 20–60 µm, with bulk density 0.30–0.55 g/mL and tapped density 0.40–0.70 g/mL. FZNT-02-D for direct compression is micronized to D90 ≤20 µm and is supplied with bulk density 0.20–0.40 g/mL, which typically requires flow-aid addition to prevent ratholing in a tablet press hopper. FZNT-03-I for injectable formulation development is milled under reduced bioburden controls and is not terminally sterilized as an API. For capsule and tablet manufacturing, the API is pre-blended with a diluent at 1:1 w/w geometric dilution before high-shear mixing to reduce segregation; blend uniformity is assessed by stratified sampling and USP <905> criteria. In wet granulation, purified water is added to a binary pre-blend of API, lactose monohydrate, and binder, with granulation endpoint controlled by impeller torque or power consumption on the high-shear mixer. Drying in a fluid-bed dryer should maintain product temperature below 40°C unless stability-indicating data support a higher temperature; inlet air temperature 50–60°C is a common starting point for granule drying. Granules are screened through 0.8–1.2 mm screens before lubrication and compression. Direct compression blends are compressed on a rotary tablet press at target hardness 60–120 N depending on tablet geometry, but hardness specifications must be derived from disintegration and dissolution data, not press convenience.
Fezolinetant-containing oral formulations require dissolution testing as a release method only after the discriminatory power of the dissolution procedure has been demonstrated. pH solubility dependence and the effect of sodium lauryl sulfate concentration in media should be investigated during method development. For a BCS-based solubility classification, published data for this specific configuration is limited; therefore the dissolution method cannot be assumed from chemical structure alone. The approved oral commercial product is a tablet, but capsule and granule dosage forms can be developed using the same API when blend uniformity and dissolution equivalence are demonstrated against the intended clinical reference.
Fezolinetant differs from menopause hormone therapy because it does not supply estradiol, conjugated equine estrogens, or a progestogen. Receptor profiling shows no direct estrogen receptor alpha or beta agonist activity, and the approved prescribing information does not list endometrial stimulation or estrogen-dependent malignancy as pharmacologic effects. The clinical target is the neurokinin 3 receptor on KNDy neurons in the arcuate nucleus, where neurokinin B signaling is reduced rather than estrogen-mediated feedback pathways being replaced. This distinction is operationally relevant in the API specification because estrogenic impurities are not part of the control strategy, whereas chiral purity and related substances from the synthetic route are of primary concern. Compared with low-dose paroxetine mesylate used for vasomotor symptoms, fezolinetant acts by a different receptor pathway and therefore has a different adverse effect boundary. The serotonergic side effect profile associated with selective serotonin transporter inhibition is not the primary monitoring concern; instead, hepatic transaminase elevations are the key safety signal. Baseline alanine aminotransferase, aspartate aminotransferase, and total bilirubin are obtained before treatment initiation, repeated at 3 months, 6 months, and 9 months after initiation, and followed periodically in patients with elevations. Co-administration with strong CYP1A2 inhibitors is contraindicated because fezolinetant clearance depends substantially on CYP1A2-mediated oxidation. This hepatic and CYP1A2 interaction profile differentiates fezolinetant from over-the-counter botanical vasomotor preparations, which are not characterized by the same receptor selectivity or the same regulatory evidence base.
| Attribute | Fezolinetant | Menopause hormone therapy | Low-dose paroxetine mesylate |
|---|---|---|---|
| Primary receptor target | Neurokinin 3 receptor antagonist | Estrogen receptor alpha/beta agonist | Serotonin transporter inhibitor |
| Direct estrogenic activity | None demonstrated | Present | None demonstrated |
| Approved oral dose | 45 mg once daily | Variable by product and indication | 7.5 mg once daily |
| Principal safety monitoring | Baseline and periodic ALT, AST, and total bilirubin | Thromboembolic risk, endometrial risk, breast cancer risk | Serotonergic adverse effects, CYP2D6 drug interactions |
| Key interaction boundary | Strong CYP1A2 inhibitors contraindicated | Not uniform; product-specific | CYP2D6 inhibition and serotonergic drug interactions |
| Regulatory status for vasomotor symptoms | FDA-approved oral product | Approved but with different benefit-risk population | FDA-approved lower-dose formulation |
The API-level difference is that fezolinetant is a single enantiomer with chiral control required by chiral HPLC or equivalent method. In contrast, estradiol hemihydrate or micronized estradiol is a naturally occurring steroid controlled by steroidal impurity profiles under compendial monographs where applicable. Low-dose paroxetine mesylate is a salt of a chiral base; paroxetine has compendial monographs and is controlled for related substances, residual solvents, and chiral identity. Fezolinetant therefore presents a more recent non-compendial control challenge: the manufacturer must generate and justify acceptance criteria rather than defaulting to a compendial test battery. This does not reduce the rigor; it increases the need for ICH Q11 development history, route-specific impurity mapping, and stability-qualified analytical procedures.
For injectable formulation development, FZNT-03-I is a micronized grade with reduced bioburden and bacterial endotoxin limit based on the intended maximum parenteral dose per USP <85>. The API is not intrinsically sterile; terminal sterilization or aseptic filtration of the formulated solution is required. Published data for injectable fezolinetant configurations are limited; the approved reference product is an oral tablet. Solubility in aqueous buffers should be determined empirically as a function of pH, tonicity modifier, and cyclodextrin content, because solubility in pure water cannot be assumed from the oral absorption profile. If a solution dosage form is developed, filter compatibility should be confirmed with 0.22 µm PVDF or PES membranes because some neutral hydrophobic drug substances adsorb to filter surfaces and reduce recoverable potency. Terminal autoclaving at 121°C should not be used without stability-indicating data for degradation products; if steam sterilization is required, the effect on related substances and chiral purity must be monitored. For lyophilized injectable presentations, the API should be dissolved and sterile-filtered before lyophilization, and the reconstituted solution should be protected from light if photodegradation is observed during forced degradation studies. The oral grades should be stored in tightly closed containers protected from moisture, with controlled room temperature storage at 20–25°C and excursions permitted to 15–30°C only when justified by stability data under the chosen container closure system. Pre-drying before formulation is required if water content exceeds the release limit or if the API is exposed to ambient relative humidity above 60% for prolonged transfer operations.