| HS Code | 461086 |
| Product Name | Apalutamide Pharma Grade API |
| Api Name | Apalutamide |
| Synonyms | ARN-509; JNJ-56021927; Erleada |
| Chemical Name | 4-[7-[6-cyano-5-(trifluoromethyl)pyridin-3-yl]-8-oxo-6-sulfanylidene-5,7-diazaspiro[3.4]octan-5-yl]-2-fluoro-N-methylbenzamide |
| Cas Number | 956104-40-8 |
| Molecular Formula | C21H15F4N5O2S |
| Molecular Weight | 477.44 g/mol |
| Grade | Pharma Grade / API Grade / GMP |
| Purity | ≥99.0% (HPLC) |
| Appearance | White to off-white crystalline powder |
| Solubility | Practically insoluble in water; soluble in DMSO and methanol |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Routes Of Administration | Oral, Injectable |
| Therapeutic Category | Androgen receptor inhibitor; antineoplastic |
| Mechanism Of Action | Binds to androgen receptor ligand-binding domain, inhibiting nuclear translocation and DNA binding |
| Target | Androgen Receptor (AR) |
| Indication | Non-metastatic castration-resistant prostate cancer; metastatic castration-sensitive prostate cancer |
| Storage Conditions | Store in a cool, dry place, protected from light and moisture; recommended 2–8°C for long-term storage |
| Shelf Life | 24 months when stored properly |
| Packaging | Double polyethylene bags in fiber drum; customizable packaging |
| Handling Precautions | Use personal protective equipment; avoid inhalation and contact |
| Regulatory Status | Approved drug API; GMP manufactured |
As an accredited Apalutamide 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 | Apalutamide Pharma Grade API, 25 kg, packed in double polyethylene-lined fiber drums for tablets, capsules, granules, oral and injectable use. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Apalutamide Pharma Grade API for tablet, capsule, granule, oral, and injectable forms; palletized, sealed, labeled. |
| Shipping | Apalutamide Pharma Grade API is shipped in sealed, light-resistant, tamper-evident containers under cGMP/GDP conditions. Maintain temperature per stability data, typically 20–25°C, protected from moisture and contamination. Include CoA, SDS, and batch documentation. Handle as potent pharmaceutical material; non-hazardous unless otherwise classified. Follow all applicable regulatory transport requirements. |
| Storage | Store Apalutamide Pharma Grade API in tightly closed, original containers in a cool, dry, well-ventilated area, protected from light and moisture. Maintain controlled room temperature 20–25°C (68–77°F), with excursions 15–30°C. Keep away from heat, ignition sources, and incompatible materials. Use dedicated, labeled containers suitable for oral and injectable use; follow cGMP and manufacturer instructions. |
| Shelf Life | Apalutamide API shelf life typically 24–36 months when sealed, protected from light/moisture, stored at controlled room temperature, per manufacturer stability data. |
In the only registered oral solid drug product, apalutamide is not dry-blended as neat crystalline powder but is first converted into an amorphous solid dispersion with hypromellose acetate succinate because the free base remains practically insoluble across the physiological pH range evaluated during gastrointestinal transit. The approved finished tablet carries 60 mg apalutamide per unit and lists croscarmellose sodium, colloidal silicon dioxide, hypromellose acetate succinate, magnesium stearate, microcrystalline cellulose, and silicified microcrystalline cellulose among the core components, although the public label does not provide quantitative excipient mass. The formulation addition ratio is therefore verifiable only as the labelled dose of 60 mg apalutamide per tablet; confidential batch records govern the exact weight fraction. In external quality-by-design screening for this class of HPMC-AS amorphous solid dispersions, drug loadings in the spray-dried intermediate are commonly challenged between 20% w/w and 40% w/w, while the final tablet core active fraction typically falls between 15% w/w and 30% w/w after blending with microcrystalline cellulose and disintegrant, with published data for apalutamide-specific percentage availability limited. The downstream manufacturing sequence comprises spray drying of a solvent-laden feed, secondary drying to a loss-on-drying value not exceeding 2.0% w/w, dry blending, lubrication with magnesium stearate at 0.25–1.0% w/w for 3–5 min, tablet compression on a rotary press, and aqueous film coating to a weight gain of 2–4% w/w. Process excursions on production-scale rotary machines are observed when the spray-dried powder is not conditioned below 40% RH; static charging and inconsistent hopper flow produce weight variation outside the release limits of USP <905>. Release testing is anchored to ICH Q1A(R2) stability protocols, ICH Q3D elemental impurities limits, USP <711> dissolution using surfactant-selected media according to USP <1092>, and USP <905> uniformity of dosage units. The terminal dosage form is the immediate-release film-coated tablet for once-daily oral administration at a standard dose of 240 mg administered as four tablets; no compression-coated, enteric, or modified-release version is approved.
| Attribute | Reference standard | Acceptance anchor / status |
|---|---|---|
| Uniformity of dosage units | USP <905>, Ph. Eur. 2.9.40 | Acceptance value ≤ 15.0 |
| Dissolution | USP <711>, Ph. Eur. 2.9.3 | Case-specific Q value established via USP <1092> |
| Friability | USP <1216> | ≤ 1.0% weight loss |
| Assay | FDA 21 CFR 211.110 | 90.0–110.0% label claim |
| Elemental impurities | ICH Q3D | PDE-based limit for oral route |
| Stability monitoring | ICH Q1A(R2) | Long-term, intermediate, and accelerated conditions |
For capsule filling operations, the amorphous solid dispersion powder presents a low bulk density and moderate electrostatic charge that cannot be addressed by simply transferring the tableting blend into a hard shell. The capsule-specific downstream process therefore begins with pre-blending the spray-dried intermediate with colloidal silicon dioxide as a glidant, adding a disintegrant such as croscarmellose sodium, and then lubricating with magnesium stearate at the same low-shear intensity used for tablet lubrication; excessive shear or over-lubrication beyond 5 min can produce hydrophobic surface coatings and reduce dissolution release under USP <711>. Compliance for this oral solid dosage track falls under FDA 21 CFR 211.110 in-process sampling, USP <905> uniformity of dosage units, USP <711> dissolution, ICH Q1A(R2) stability, and ICH Q3D elemental impurities, with capsule shell integrity assessed by visual inspection and moisture content. The addition ratio is determined by the target unit dose of 60 mg apalutamide per capsule; published data for apalutamide-specific capsule fill mass are limited, but hard capsule filling of low-density amorphous solid dispersion powders generally requires a total fill mass of 180–300 mg for a size 0 shell, yielding an active weight fraction of 20–33% w/w. When a lower unit dose is required for clinical bridging, the active fraction would decrease proportionally unless the total fill mass is reduced. The filling process is executed on dosator or tamping-pin capsule machines operating under low-humidity conditions; spray-dried intermediate should not be exposed to relative humidity above 60% RH for more than 4 h, and terminal capsule seals should be qualified for moisture ingress if the final product will be packed in HDPE bottles with desiccant. The terminal product type for this route is a hard-shell oral capsule, either gelatin or HPMC, with the same immediate-release performance expectation as the film-coated tablet but with no commercial apalutamide capsule currently registered.
When direct compression of a 60 mg strength core becomes impractical because of low bulk density, high elastic recovery, or feed segregation, dry granulation by roller compaction is introduced to densify the amorphous solid dispersion-containing powder before final tableting. This granulation path is relevant to oral granule intermediate production because it converts the spray-dried dispersion into free-flowing, compressible granules with reduced dust and controlled particle size distribution. The active addition ratio remains fixed at 60 mg apalutamide per unit dose in the downstream tablet; on a mass basis, the granulated blend typically contains 20% w/w to 35% w/w apalutamide when the roller-compacted fraction is diluted with extragranular filler, but apalutamide-specific public batch data are not available to confirm a narrower range. The production process comprises pre-blending, roller compaction at roll pressures in the 4–12 kN/cm range, roll gap control between 1.0 mm and 2.0 mm, milling through a screen of 0.8–1.5 mm, post-mill blending, and lubrication with magnesium stearate. Sieve analysis of the resulting granules typically targets a D50 in the 150–850 µm interval, with loss on drying after granulation maintained below 2.0% w/w. In production-scale roller compactors with horizontal feed, granule hardness and porosity are monitored by bulk and tapped density rather than by particle hardness alone; density variations greater than ±0.05 g/cm³ across the batch can lead to weight variation at the press and later content uniformity failures under USP <905>. Compliance is maintained under FDA 21 CFR 211.110, USP <711>, USP <905>, ICH Q1A(R2), and ICH Q3D. The terminal product from this operation is either a granule intermediate that is subsequently compressed into tablet cores or, where regional regulatory filing supports it, a bulk oral granule packed in unit-dose sachets; no commercial apalutamide granule sachet is currently identified.
No approved injectable dosage form of apalutamide exists in the United States, European, or Japanese regulatory records; the only registered terminal product is an oral film-coated tablet, and the public development literature does not contain validated sterile suspension or solution compositions. The fundamental constraint is the practically insoluble character of the free base in aqueous media, which requires either nanomilling, cyclodextrin complexation, lipid emulsion, or pH adjustment in a permissible range, and the parenteral route only raises the bar because every excipient must be injectable-grade and the finished formulation must pass sterility, endotoxin, and particulate matter testing. The applicable compliance framework for any injectable development would include USP <1> injections, USP <71> sterility tests, USP <85> bacterial endotoxins, USP <788> particulate matter in injections, ICH Q3D for parenteral elemental impurities, and 21 CFR 211.94 container closure systems, but none of these method applications can be claimed for apalutamide because no marketed parenteral product exists. The addition ratio cannot be established from public data; published data for this specific configuration is limited. Standard parenteral formulations for poorly water-soluble antineoplastic agents often aim for a drug concentration between 10 mg/mL and 50 mg/mL in the ready-to-use or reconstituted presentation, but the measured solubility of apalutamide without solubilising excipients is far below that interval, making the range aspirational rather than validated. If a nanosuspension route were pursued, the downstream process would involve high-pressure homogenisation at 1000–1500 bar with subsequent particle size reduction to a D90 below 500 nm, followed by aseptic filling or terminal moist-heat sterilisation where thermal stability permits; lyophilisation would require a collapse-free cake with a reconstitution time below 2 min. However, the absence of apalutamide-specific solubility data in parenteral vehicles, the risk of Ostwald ripening in a nanosuspension, and the lack of a validated terminal sterilisation cycle mean that these unit operations cannot be transferred directly from oral solid dosage processing. The terminal product type, if development were successfully completed, would be either a lyophilized cake for reconstitution or a sterile aqueous suspension, but at present no such terminal product is registered or supported by publicly available stability data.
| Parenteral attribute | Applicable standard | Data availability for apalutamide |
|---|---|---|
| Sterility | USP <71>, Ph. Eur. 2.6.1 | No registered parenteral formulation; method validation absent |
| Bacterial endotoxins | USP <85>, Ph. Eur. 2.6.14 | Applicable to injectable route; no public monograph data |
| Particulate matter | USP <788> | Method applicable; apalutamide-specific limits not published |
| Elemental impurities | ICH Q3D | Parenteral PDE route; no marketed product data |
| Container closure | 21 CFR 211.94 | No qualified stopper/vial system in public records |
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Apalutamide Pharma Grade API is supplied under the product codes APL-APA-01, APL-APA-02, and APL-APA-03. These materials are controlled for use in tablets, capsules, granules, oral suspensions, and injectable development. The active substance is a nonsteroidal androgen receptor inhibitor with the molecular formula C21H15F4N5O2S, molecular weight 477.43 g/mol, and CAS Registry Number 956104-40-8. It appears as a white to off-white crystalline powder. The compound is practically insoluble in aqueous media across physiological pH, which makes particle-size reduction and wetting/dispersion strategy the main formulation variables for oral solid and injectable dosage forms. The approved oral tablet strength is 60 mg; capsule, granule, and injectable presentations are not described in approved labeling and must be qualified independently under current good manufacturing practice, including FDA 21 CFR 211.84 for component testing and FDA 21 CFR 211.160 for laboratory controls.
Product code APL-APA-01 is the air-jet-milled oral solid grade. Particle-size distribution is controlled by laser diffraction using ISO 13320:2020 with D90 ≤25 µm and D50 3–10 µm. APL-APA-02 is the unmicronized oral granulation grade; it has a larger D90 ≤75 µm and is selected when particle size reduction will be performed during wet granulation or roller compaction. APL-APA-03 is the injectable-development grade with bacterial endotoxin controlled to <0.5 EU/mg by Ph. Eur. 2.6.14 and bioburden controlled to ≤100 CFU/g. APL-APA-03 is not sterile; the finished injectable product must be sterilised by a validated process or processed aseptically after formulation.
Release controls are based on the impurity threshold framework of ICH Q3A(R2), residual solvent limits of ICH Q3C(R8), and elemental impurity limits of ICH Q3D(R2). Assay by HPLC with ultraviolet detection is controlled at 98.0–102.0% on the anhydrous and solvent-free basis. Total related substances are limited to ≤1.0%; any unspecified individual impurity is limited to ≤0.10%. Residual solvent limits include methanol ≤3000 ppm, N,N-dimethylformamide ≤880 ppm, tetrahydrofuran ≤720 ppm, and ethanol ≤5000 ppm. Elemental impurities by inductively coupled plasma mass spectrometry follow ICH Q3D Option 1, with palladium ≤10 µg/g, nickel ≤20 µg/g, and arsenic ≤15 µg/g. Water content by Karl Fischer titration is ≤0.5%. Crystalline identity is confirmed by X-ray powder diffractometry against a controlled reference diffractogram. Method validation for assay and related substances follows ICH Q2(R1); system suitability includes resolution between apalutamide and its closest specified impurity.
| Attribute | Method / standard | Representative limit |
|---|---|---|
| Assay | HPLC-UV, ICH Q2(R1) | 98.0–102.0% |
| Unspecified impurity | ICH Q3A(R2) | ≤0.10% |
| Total impurities | ICH Q3A(R2) | ≤1.0% |
| Methanol | ICH Q3C(R8) | ≤3000 ppm |
| N,N-dimethylformamide | ICH Q3C(R8) | ≤880 ppm |
| Palladium | ICP-MS, ICH Q3D(R2) | ≤10 µg/g |
| Particle size D90, micronized | ISO 13320:2020 | ≤25 µm |
| Bacterial endotoxin, injectable grade | Ph. Eur. 2.6.14 | <0.5 EU/mg |
Solid-state analysis is performed by X-ray powder diffractometry and differential scanning calorimetry. The melting endotherm is controlled against a reference crystalline form; solvated or recrystallised variations are considered out of specification because they alter dissolution and processing behaviour. Surface area is reported for the micronized grade because it correlates with dissolution rate in the low-solubility formulation environment. Bulk density and tapped density are also reported, as both parameters influence die fill and capsule fill weight. The specification described here is a release specification, not a guarantee of performance in every finished formulation. The API manufacturer provides batch-specific certificates of analysis and a technical dossier containing method validation summaries, forced degradation data, and residual solvent and elemental impurity profiles. The batch-to-batch variability of the micronized grade is controlled through process validation and annual product quality review under ICH Q7.
At production scale, the unmicronized APL-APA-02 powder is cohesive and does not flow reliably through gravity-fed rotary tablet press hoppers. Direct compression without a granulation step has produced weight variation exceeding USP <905> acceptance criteria when tableting speed exceeds approximately 40 rpm on a 10-station rotary press equipped with standard B-tooling; published production-scale data for this specific configuration is limited. Pre-blending with microcrystalline cellulose and colloidal silicon dioxide improves flow but does not remove the need for forced feed frames or vacuum-assisted die filling. Pre-drying at 40 ±5 °C for 4 h is recommended when ambient relative humidity exceeds 60% because the powder becomes cohesive and may adhere to punch faces and capsule dosator surfaces. Apalutamide should not be blended with strong oxidising agents or with acidic excipients that promote hydrolytic degradation unless forced degradation studies support compatibility.
When direct compression is not feasible, the tablet formulation route shifts to either dry roller compaction or high-shear wet granulation. Wet granulation in a high-shear granulator typically uses povidone K30 at 2–5% w/w binder solids and either water or an ethanol-water mixture. The endpoint is controlled by impeller torque or current; wet mass is passed through a 1.0–1.5 mm screen and dried at 50–60 °C until loss on drying is ≤2.0%. The dried granules are milled and blended with disintegrant and lubricant. For immediate-release tablets, dissolution is evaluated with USP <711> apparatus II at 75 rpm in pH 1.2, 4.5, and 6.8 media; the low aqueous solubility of apalutamide means that the dissolution profile is highly sensitive to particle size and granule porosity. For capsules, the dried granules are filled on a dosator or tamping-pin encapsulation machine; fill weight uniformity is assessed by USP <905> or current pharmacopoeial equivalent. Roller compaction is preferred when hydrolytic degradation must be minimised. Ribbons are compressed to a target density that produces a milled granule D50 below 500 µm; fines below 75 µm are limited to ≤35% because increased fines reduce flow and can produce capping or weight variation.
Granule products for sachet or suspension require additional wetting and suspending agents because apalutamide is practically insoluble. Aqueous suspensions are developed with polysorbate- or poloxamer-based wetting agents and viscosity-building polymers; homogenisation at high shear reduces the mean particle size and improves dissolution. The granule blend is dried to moisture ≤2.0% and packaged with desiccant if moisture-sensitive excipients are present. Flow and bulk density are controlled before filling because low-density granules can produce unacceptable fill variation in volumetric sachet fillers. Tablet hardness and friability are tested by crushing strength method in Ph. Eur. 2.9.8 and friability method in Ph. Eur. 2.9.7; finished oral solid products are assessed for dissolution, assay, and impurities according to current pharmacopoeial requirements.
For oral suspension or powder for suspension, the API is first dispersed in a vehicle containing a wetting agent such as polysorbate 80 or poloxamer 188. A viscosity-building polymer such as hypromellose or xanthan gum is added to retard sedimentation. The pH of the vehicle should be selected after solubility-screening in media from pH 2.0 to 7.5; elevated pH may reduce solubility further and should be avoided unless a solubilising carrier is present. Chemical stability studies for solution or suspension dosage forms should follow ICH Q1A(R2). Taste-masking agents are required for oral suspension because apalutamide can produce a bitter taste in aqueous dispersion.
Injectables based on apalutamide require a different control strategy because the API is practically insoluble in aqueous media and sterile filtration of a simple solution is not feasible. APL-APA-03 is supplied with reduced bioburden and endotoxin, but the formulated product must be processed aseptically from this point. A nanosuspension produced by high-pressure homogenisation can be considered for parenteral use; the API particle size should be reduced to D50 below 500 nm and sterility assured by aseptic processing because terminal steam sterilisation data for apalutamide is limited. Alternatively, a lipid or surfactant-based carrier can be used, but the finished product must be assessed for hemolysis, injection-site tolerance, and sterility per Ph. Eur. 5.1.1 and current pharmacopoeial injectable tests. The API is not intended for direct injection as a powder.
Apalutamide differs from enzalutamide and bicalutamide in receptor pharmacology, central nervous system distribution, and clinical dose. Apalutamide is a second-generation nonsteroidal androgen receptor inhibitor that binds the ligand-binding domain and inhibits androgen receptor nuclear translocation, DNA binding, and androgen-mediated transcription. Unlike bicalutamide, apalutamide does not show partial agonist activity in non-clinical models. Published receptor-binding studies show that apalutamide and enzalutamide both bind the wild-type androgen receptor with high affinity, but apalutamide has a lower brain-to-plasma exposure than enzalutamide in rodent distribution studies. That difference is relevant to the seizure signal observed in the clinical development programmes. The approved oral dose of apalutamide is 240 mg once daily; enzalutamide is 160 mg once daily; bicalutamide is 50 mg once daily.
| Parameter | Apalutamide | Enzalutamide | Bicalutamide |
|---|---|---|---|
| Androgen receptor action | Full antagonist | Full antagonist | Partial agonist in some models |
| Approved daily oral dose | 240 mg | 160 mg | 50 mg |
| Approved tablet strength | 60 mg | 40 mg | 50 mg |
| Brain-to-plasma exposure | Lower than enzalutamide | Higher than apalutamide | Not consistently reported |
| Indication examples | NM-CRPC, mCSPC | mCRPC, NM-CRPC, mCSPC | metastatic prostate cancer |
For formulation development, the relevant differences between apalutamide and enzalutamide are not limited to receptor binding. Apalutamide has a lower aqueous solubility and a larger clinical dose, which means a 240 mg daily dose may require more than one dosage unit or a higher drug-load tablet. Enzalutamide is formulated as 40 mg soft gelatin capsules or tablets; apalutamide is formulated as 60 mg tablets. The difference in dose and poor solubility makes apalutamide more dependent on particle-size reduction and dispersion than bicalutamide, which is typically used at 50 mg once daily. Direct substitution of one API into the other’s formulation is not appropriate without stability, dissolution, and excipient compatibility studies.