| HS Code | 826178 |
| Product Name | Megestrol Veterinary Grade API |
| Chemical Entity | Megestrol acetate |
| Grade | Veterinary |
| Chemical Class | Synthetic progestogen/progestin |
| Molecular Formula | C24H32O4 |
| Molecular Weight | 384.51 g/mol |
| Appearance | White to off-white crystalline powder |
| Solubility | Practically insoluble in water; sparingly soluble in alcohol; soluble in chloroform and acetone |
| Melting Point | 214-220°C |
| Mechanism Of Action | Inhibits pituitary gonadotropin secretion, suppressing oestrus and ovulation |
| Therapeutic Category | Progestational hormone |
| Veterinary Indications | Oestrus suppression, pseudopregnancy control, and adjunctive hormonal therapy in small animals |
| Target Species | Dogs and cats |
| Compatible Dosage Forms | Tablets, injections, capsules, powders, granules, premix, solutions |
| Storage Conditions | Store in tightly closed containers in a cool, dry place; protect from light and moisture |
As an accredited Megestrol Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in sealed, light-resistant containers with tamper-evident closures, available in 25 kg drums, suitable for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Container Loading (20′ FCL) | Container loading of Megestrol Veterinary Grade API into a 20′ FCL, securely packed for transport of various formulations. |
| Shipping | Megestrol Veterinary Grade API ships in sealed, light-protected containers with tamper-evident seals, compliant with international transport regulations. Cold-chain or temperature-controlled options available. Full documentation, safety data sheets, and customs paperwork provided for tablets, injections, capsules, powders, granules, premix, or solutions. Ensure secure, traceable global delivery. |
| Storage | Store in a cool, dry, well-ventilated area, protected from light, moisture, and heat. Keep container tightly closed when not in use. Avoid exposure to direct sunlight and incompatible materials. Maintain room temperature, typically 15–30°C. Use clean, dedicated equipment during handling to prevent contamination. Follow animal-safety guidelines and regulatory requirements for veterinary APIs. |
| Shelf Life | Megestrol Veterinary Grade API has a shelf life of 36 months when stored in original, tightly sealed containers under cool, dry, dark conditions. |
Megestrol acetate for canine estrus postponement, pseudopregnancy, and benign prostatic hypertrophy is manufactured as an immediate-release tablet in which the dissolution rate is controlled primarily by the particle size distribution of the API and the deaggregation behavior in the intestinal lumen rather than by pH-adjusted solubility. At production scale, a 5 mg dose in a 100 mg core yields an active fraction of 5.0% w/w; a 20 mg dose in a 200 mg core yields 10.0% w/w. These percentages are arithmetic values derived from the registered tablet mass and are not fixed pharmacopeial limits. The formulation is typically processed by high-shear wet granulation with the API in the intragranular phase to minimize segregation during tablet press transfer. Binder addition is stopped when a wet mass with a controlled retained fraction on a 0.500 mm sieve is formed; the granulate is dried in a fluid-bed dryer until loss-on-drying reaches the registered range, which is a more stable endpoint than fixed impeller power because lot-to-lot excipient moisture shifts the torque signal before the granulation is complete. Published product-specific data for a fixed impeller power target in megestrol acetate granulation are limited.
The dried granulate is calibrated, blended with extragranular disintegrant and lubricant, and compressed on a rotary tablet press. In-process controls include tablet hardness, thickness, friability according to USP <1216> with a limit of 1.0% after 100 revolutions, disintegration according to USP <701>, and dissolution according to USP <711>. Release uniformity is determined under USP <905> with an acceptance value not exceeding 15. Finished-product compliance follows 21 CFR 210/211; residual solvent testing aligns with ICH Q3C or VICH GL18 for the veterinary registration dossier. Terminal finished types are round, scored, film-coated 5 mg and 20 mg tablets packed in white high-density polyethylene bottles with light-resistant child-resistant closures. Film coating uses an aqueous hypromellose dispersion rather than an organic-solvent coating system, reducing residual solvent burden and supporting the ICH Q3C declaration.
In feline patients requiring dose escalation from 1.0 mg to 2.5 mg per day for anorexia or cachexia, megestrol acetate is manufactured as low-dose hard gelatin or hydroxypropyl methylcellulose capsules to permit adjustment without splitting tablets. A 1.0 mg dose in a 200 mg capsule fill produces 0.5% w/w active fraction; a 2.5 mg dose in a 170 mg fill produces 1.47% w/w; a 5.0 mg dose in a 150 mg fill produces 3.33% w/w. Low-dose capsule production uses geometric dilution or trituration before final blending; the API is first blended with lactose monohydrate in a 1:10 ratio, sieved through a 0.300 mm screen, then diluted stepwise until the final blend mass is reached in a low-shear tumble blender. Lubrication is performed with 0.5% w/w magnesium stearate, and the blend is encapsulated on a dosator or tamping-style machine. Segregation during hopper transfer is a recognized batch failure mode; the corrective action is to reduce the API-to-diluent particle size difference or to use a granulated lactose-maltodextrin carrier rather than an unprocessed direct-compression lactose. Content uniformity is assessed by USP <905>; dissolution is assessed by USP <711>; finished-product GMP follows 21 CFR 210/211. Residual solvent and elemental impurity control align with ICH Q3C and ICH Q3D. Compounded versions prepared by veterinary pharmacies fall under USP <795> rather than 21 CFR 210/211. Terminal finished products are two-piece capsules in strengths of 1 mg, 2.5 mg, and 5 mg, filled into amber glass or high-density polyethylene bottles.
| Dose strength | Unit fill mass | Calculated API fraction |
|---|---|---|
| 1.0 mg | 200 mg | 0.5% w/w |
| 2.5 mg | 170 mg | 1.47% w/w |
| 5.0 mg | 150 mg | 3.33% w/w |
Encapsulation speed and fill weight variation are monitored because the low active fraction makes fill-weight drift the dominant source of content non-uniformity; dosator-style machines with tamping pins require periodic static charge checks when ambient relative humidity exceeds 60%.
Megestrol acetate is practically insoluble in water; any injectable presentation is therefore a sterile aqueous suspension rather than a solution. For a 20 mg/mL strength the formula contains 2.0% w/v API; for a 10 mg/mL strength the fraction is 1.0% w/v. The manufacturing route begins with micronization to a suspension-grade particle size distribution, typically a D90 no greater than 5 µm, before the API is wetted with a polysorbate or lecithin wetting agent. Over-milled material can produce electrostatic aggregates that resist redispersion; under-milled material can settle rapidly and fail syringeability. The vehicle phase is prepared by dispersing sodium carboxymethylcellulose or microcrystalline cellulose–carboxymethylcellulose sodium in water with glycerin as a tonicity and viscosity modifier; the sterile micronized API is then incorporated under aseptic high-shear mixing. The sterile micronized API is prepared by validated dry heat or gamma irradiation; autoclaving the dry powder is avoided because the combination of moisture and heat can fuse micronized particles into agglomerates that no longer meet the D90 specification. Moist-heat terminal sterilization of the finished suspension may accelerate flocculation, crystal growth, and irreversible caking; therefore aseptic processing of the sterile API, sterile vehicle, and sterile container-closure system is the preferred route. Release testing includes sterility by USP <71>, bacterial endotoxins by USP <85>, particulate matter by USP <788>, and uniformity of dosage units by USP <905>. The finished product is filled into amber glass vials with rubber stoppers and sealed under controlled humidity. Published product-specific stability data for veterinary megestrol acetate injectable suspensions are limited; release and shelf-life criteria therefore come from the registered dossier rather than from compendial generic limits.
| Release attribute | Method or clause | Control basis |
|---|---|---|
| Sterility | USP <71> | No growth after compendial incubation |
| Bacterial endotoxins | USP <85> | Limit per registered monograph |
| Particulate matter | USP <788> | Monographed limits for injections |
| Uniformity of dosage units | USP <905> | Acceptance value ≤ 15 |
Injectable megestrol acetate is not a high-volume aseptic fill; batch sizes are moderate and require line clearance after each campaign because residual suspension film around fill needles can impair weight control and introduce cross-batch contamination.
For feline behavioral indications such as urine marking and psychogenic alopecia, megestrol acetate is formulated as an oral suspension because required doses can fall below 1.0 mg and tablet fragment splitting produces unacceptable weight variability. A 20 mg/mL oral suspension corresponds to 2.0% w/v; a 40 mg/mL strength corresponds to 4.0% w/v. The vehicle is prepared by hydrating microcrystalline cellulose and carboxymethylcellulose sodium in purified water, adding glycerin as a sweetening and viscosity agent, and incorporating sodium benzoate or potassium sorbate as a preservative. The API is dispersed under a rotor–stator homogenizer to deaggregate the micronized solid, then the finished suspension is filled into amber polyethylene terephthalate or glass bottles with a syringe-compatible adapter. Fill volume is checked according to Ph. Eur. 2.9.5 or equivalent; preservative efficacy is confirmed by Ph. Eur. 5.1.3 or USP <51>. Manufactured oral suspensions follow 21 CFR 210/211, while extemporaneous compounded liquids prepared from API powder follow USP <795>; elemental impurities are controlled by ICH Q3D. The product category may be listed as an oral solution in regulatory dossiers, but a true solution at therapeutic concentration is not achievable because of the low aqueous solubility of megestrol acetate; the term “solution” is a legacy classification rather than a physicochemical description. Terminal finished products are multi-dose oral suspensions in 20 mg/mL and 40 mg/mL strengths, with shelf-life limited by redispersibility and preservative efficacy rather than by API chemical degradation alone.
Powder, granule, and premix presentations of megestrol acetate support in-clinic preparation of capsules, oral suspensions, and dose-adjusted tablets when licensed finished products are not available or when a veterinarian specifies a patient-specific strength. A 5 mg/g trituration corresponds to 0.5% w/w; a 10 mg/g trituration corresponds to 1.0% w/w; a 25 mg/g premix corresponds to 2.5% w/w. The powder is prepared by geometric dilution using lactose monohydrate or pregelatinized starch, passing the mixture through a 0.180 mm to 0.300 mm sieve between dilution steps. If granulation is required to prevent segregation during bulk transport, the blend is granulated with purified water or a starch paste and dried in a fluid-bed dryer at a conservative inlet air temperature; published thermal stability data for megestrol acetate in low-moisture premix matrices are limited, so drying temperature is justified by forced-degradation studies in the registration batch. Final filling into sachets or jars is conducted under controlled relative humidity, and residual moisture is determined by Karl Fischer titration. Non-sterile compounding standards include USP <795>; if the material is handled as a potential occupational hazard, containment and personal protective equipment controls align with USP <800>. Terminal finished types are unit-dose powder sachets, bulk trituration jars, and granulated premix vessels intended for extemporaneous suspension or capsule filling in veterinary practice.
Batch release for a powder trituration is dominated by blend uniformity and microbial limits rather than dissolution; the upstream API particle size should be controlled to D90 ≤10 µm to ensure acceptable distribution across the diluent surface. At relative humidity above 60%, lactose-based triturations can form agglomerates around the API, producing content uniformity failures in low-fill-weight capsules.
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Megestrol acetate is supplied as a veterinary-grade active pharmaceutical ingredient for formulation into tablets, injectable suspensions, capsules, oral powders, granules, premixes, and non-aqueous solutions. The substance is the 17α-acetoxy-6-methylpregna-4,6-diene-3,20-dione; its CAS registry number is 595-33-5, its molecular formula is C24H32O4, and its molecular mass is 384.51 g/mol. The compendial powder is an off-white to cream-colored crystalline solid with low aqueous solubility. The melting range is approximately 213–217 °C, which is well above the inlet air setpoints used in fluid-bed drying and above ordinary feed-processing temperatures. Three API grades are generally distinguished by dosage form: a non-micronized grade for granules and premixes, a micronized grade for low-dose tablets and hard capsules, and an aseptic-micronized grade for injectable suspensions. The grade designation is manufacturer-specific, but each grade is the same registered substance differentiated by particle-size distribution, endotoxin control, and residual solvent clearance.
Because the API is practically insoluble in water, particle-size reduction is the primary formulation lever rather than salt selection. The material is not a soluble salt; it is the neutral 17-acetate ester. This places dissolution rate and content uniformity under direct particle-size control. Compendial identification is performed by mid-infrared absorption spectrophotometry and HPLC retention time. Assay and related substances are determined by stability-indicating liquid chromatography under USP <621> or Ph. Eur. 2.2.29. The powder properties relevant to solid dosage design include bulk density, tapped density, Hausner ratio, and compressibility index under USP <616> Method I and Method II. Particle-size distribution is measured by laser diffraction under USP <429> or by optical microscopy under USP <776> for the non-micronized grade. Loss on drying is controlled under USP <731> or Ph. Eur. 2.2.32. Where an injectable grade is released, bacterial endotoxin and sterility tests are added as described below.
Polymorphic form is controlled by X-ray powder diffraction under USP <941> because comminution can generate amorphous domains on particle surfaces. The amorphous fraction is a release-relevant variable because it alters water uptake and dissolution behavior in a low-solubility system. In a micronized grade, jet milling produces a particle population with a Dv50 often targeted in the single-digit micrometre range; the exact Dv90 is dossier-specific and is not assigned by a universal monograph. Laser diffraction under USP <429> is the standard release method for micronized material, while optical microscopy under USP <776> may be used for the coarser non-micronized grade. Bulk and tapped density are measured under USP <616> Method I and Method II. The Hausner ratio and compressibility index are used as release indicators because cohesive powder flow is the principal failure mode when the non-micronized grade is substituted into direct-compression blends. For wet granulation, pre-blending with a hydrophilic filler such as lactose monohydrate and a binder solution containing povidone K30 or pregelatinized starch is employed. The drying endpoint is controlled by loss on drying under USP <731> to avoid residual moisture-mediated hydrolysis of the 17-acetate ester. Low aqueous solubility means that content uniformity in low-dose tablet formats is especially sensitive to API particle size; dry blending without sufficient shear can leave intact agglomerates that pass assay but fail content uniformity testing under USP <905>.
The structural distinction relevant to veterinary formulators is the presence of a 6-methyl-4,6-diene system in megestrol acetate rather than the 6α-methyl-4-ene system of medroxyprogesterone acetate. The additional C6–C7 double bond produces a slightly lower molecular mass and influences solid-state packing, melting behavior, and crystal habit. In practice, megestrol acetate is not automatically interchangeable with medroxyprogesterone acetate in a compounded preparation; the receptor-binding profile, duration of ovarian suppression, and approved indications differ among jurisdictions. The more saturated analogue has a different powder density and crystal habit, so direct substitution without particle-size re-characterization violates pharmaceutical equivalence. Table 2 summarizes the structural features relevant to API specification.
| Parameter | Megestrol acetate | Medroxyprogesterone acetate |
|---|---|---|
| Ring A unsaturation | 4,6-diene | 4-ene |
| C6 substituent | 6-methyl | 6α-methyl |
| Molecular mass | 384.51 g/mol | 386.52 g/mol |
| CAS registry number | 595-33-5 | 71-58-9 |
In tablet and hard-capsule processing, the low unit dose in many veterinary indications makes segregation the principal process risk, not chemical instability. The API is first de-agglomerated through an oscillating sieve or a cone mill before being loaded into a bin blender. A staged mixing sequence with lactose monohydrate, microcrystalline cellulose, and colloidal silicon dioxide is used; the glidant ratio is kept at or below 0.5% because excess silicon dioxide can coat the API and reduce dissolution. Magnesium stearate is added last and blended for a short final interval to avoid over-lubrication. Blend uniformity is tested under USP <905>. Bulk and tapped density values from USP <616> Method I and Method II are used to establish blend hold time. For capsule filling, the same powder blend is charged to an automatic capsule machine with dosing-disc or tamping-pin technology; fill weight is monitored in-process because megestrol acetate has no special electrostatic advantage over common excipients. Aqueous wet granulation is used where direct compression is not feasible; the binder solution is prepared with povidone K30, and drying is performed in a fluid-bed dryer with inlet air at 50–60 °C, below the melting range. Drying is confirmed by loss on drying under USP <731>.
Sterile injectable suspensions of megestrol acetate require an aseptic-micronized grade with bacterial endotoxin control under USP <85> or Ph. Eur. 2.6.14. The API is practically insoluble in water, so the finished preparation is usually a flocculated suspension or a non-aqueous solution. Terminal sterilization of an aqueous suspension may not be feasible for all formulations because heat can accelerate ester hydrolysis and particle aggregation; aseptic filtration of a suspension is not possible once the API is dispersed. Therefore the API is either sterilized as a dry powder by a validated method such as gamma irradiation or ethylene oxide, or it is crystallized and processed under aseptic conditions according to EU GMP Annex 1. Sterility testing follows USP <71> or Ph. Eur. 2.6.1. Particle-size distribution is qualified by laser diffraction under USP <429> to ensure that the suspended particle population remains within the syringeability specification. Wetting agents such as polysorbate 80 or sodium carboxymethylcellulose may be used to reduce particle flocculation and caking. The 17-acetate ester is sensitive to pH extremes; the formulation should avoid prolonged exposure to conditions outside approximately pH 4–7.5 at elevated temperature. For true solutions, non-aqueous vehicles or co-solvent systems are considered; published data for this specific configuration is limited, and aqueous solubility is well below that required for a single-phase injectable.
For oral powders, granules, and medicated premixes, the non-micronized grade is frequently selected because the carrier system provides sufficient bulk to mask cohesiveness. The API is loaded onto a carrier such as lactose monohydrate, corn starch, or wheat middlings by progressive geometric dilution; the premix is then mixed in a ribbon mixer or double-cone blender. Homogeneity is verified by assay of multiple sampling points, not by a single composite sample, because segregation along the blender shell is a known batch failure mode. The finished premix is passed through an oscillating sieve to break soft agglomerates before packaging. Moisture barrier packaging is required where stability data show that exposure to relative humidity above 60% increases hydrolytic degradation of the 17-acetate ester. Granulation for oral powder sachets uses the same aqueous binder approach as tablet manufacture, but the final granule particle-size distribution is tightened by analytical sieving under USP <786> to ensure uniform dispersion in drinking water or feed.
Release of the veterinary-grade API is performed under a stability-indicating HPLC method. Method validation demonstrates separation of the primary degradants: the 6-dehydro analogue, the free 17-hydroxy derivative, and oxidative ring-hydroxylated impurities. Residual solvent content is controlled under USP <467> or Ph. Eur. 2.4.24, and the solvent profile is aligned with ICH Q3C. Where ethanol or ethyl acetate is used in synthesis, class 3 residual solvent criteria apply; if dichloromethane is used in a crystallization step, a class 2 limit must be applied. Elemental impurities are assessed under USP <232> and <233> or ICH Q3D; palladium or platinum residues from catalytic hydrogenation are declared when the synthetic route includes a hydrogenation step. The test matrix in Table 1 lists the compendial methods most commonly included in a veterinary API specification.
| Test | Method | Purpose |
|---|---|---|
| Polymorphic identity | USP <941> | Detects amorphization during milling |
| Particle-size distribution | USP <429> / Ph. Eur. 2.9.31 | Controls dissolution and content uniformity risk |
| Bulk and tapped density | USP <616> Method I/II / Ph. Eur. 2.9.34 | Predicts powder flow and compression behavior |
| Loss on drying | USP <731> / Ph. Eur. 2.2.32 | Limits residual moisture and ester hydrolysis risk |
| Residue on ignition | USP <281> / Ph. Eur. 2.2.14 | Controls inorganic residues |
| Assay and related substances | USP <621> / Ph. Eur. 2.2.29 | Quantifies API content and degradants |
| Residual solvents | USP <467> / Ph. Eur. 2.4.24 | Confirms ICH Q3C compliance |
| Elemental impurities | USP <232>/<233>; ICH Q3D | Controls catalyst residues and heavy metals |
| Microbial enumeration | USP <61>/<62>; Ph. Eur. 2.6.12/2.6.13 | Applies to non-sterile oral and premix grades |
| Sterility | USP <71>; Ph. Eur. 2.6.1 | Applies to injectable grade |
| Bacterial endotoxins | USP <85>; Ph. Eur. 2.6.14 | Applies to injectable grade |
Storage of the API is specified as protected from light and controlled at room temperature, with retest intervals assigned from long-term stability chambers according to ICH Q1A. The 17-acetate ester is not compatible with strong oxidizing agents or with acidic or alkaline granulating fluids held at elevated temperature for extended periods. Aluminum foil laminate packaging is recommended to limit moisture ingress, and the API should not be repackaged into high-moisture-transmission containers without revalidation. Batch release is performed under ICH Q7 and the applicable veterinary GMP provisions, with identical chromatographic identity standards applied to non-micronized, micronized, and aseptic-micronized grades.