| HS Code | 253049 |
| Product Name | Ciclosporin Pharma Grade API |
| Chemical Name | Cyclosporine A |
| Cas Number | 59865-13-3 |
| Molecular Formula | C62H111N11O12 |
| Molecular Weight | 1202.63 g/mol |
| Grade | Pharma Grade |
| Intended Dosage Forms | Tablet, Capsule, Granule, Injection |
| Route Of Administration | Oral and Injectable |
| Appearance | White to off-white crystalline powder |
| Solubility | Soluble in ethanol, methanol, acetone; practically insoluble in water |
| Assay | 98.0% to 101.0% on dried basis |
| Storage Conditions | Store in a tightly sealed container, protected from light and moisture, at controlled room temperature |
As an accredited Ciclosporin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in sealed double polyethylene bags with aluminum foil outer, 1 kg net per drum, for oral and injectable Ciclosporin API. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with Ciclosporin Pharma Grade API, securely packed, sealed, and prepared for oral and injectable pharmaceutical manufacturing. |
| Shipping | Pharma-grade Ciclosporin API is shipped in sealed, light-protected, double-lined containers with desiccants under controlled temperature (15–25°C). Qualified GDP logistics ensures tamper-evident handling and complete chain-of-custody documentation. Shipments comply with international pharmaceutical transport regulations, with immediate dispatch to preserve stability and integrity. |
| Storage | Store Ciclosporin Pharma Grade API in its original, tightly sealed container, protected from light and moisture. Store in a cool, dry, well-ventilated area at controlled room temperature (15–30°C), away from heat, sparks, and incompatible substances. Avoid prolonged exposure to air or humidity. Use appropriate handling precautions to maintain purity and stability throughout storage. |
| Shelf Life | Shelf life: 24 months when stored at controlled room temperature, protected from light and moisture in original container. |
Soft gelatin capsule processing with Ciclosporin Pharma Grade API does not proceed by dry-powder filling. The API is a cyclic undecapeptide of molecular mass 1202.61 g/mol, practically insoluble in water with an aqueous solubility near 0.04 mg/mL at 25 °C, and it requires a lipid-based preconcentrate to generate a kinetically stable microemulsion upon contact with gastrointestinal fluid. The fill vehicle is formulated in the working range of 10-30% w/w medium-chain triglyceride or caprylic/capric triglyceride as the lipophilic phase, 20-50% w/w macrogol glycerol hydroxystearate or polyoxyethylated castor oil as the hydrophilic surfactant, and 10-30% w/w absolute ethanol/propylene glycol as the co-solvent; the API loading in the fill mass is typically 10-20% w/w. Phase behavior is assessed by dispersing the preconcentrate into simulated gastric fluid pH 1.2 without enzyme and simulated intestinal fluid pH 6.8, then measuring droplet size by dynamic light scattering according to ISO 22412:2017. A microemulsion is considered acceptable only if the z-average droplet diameter remains below 50 nm after 1:50 aqueous dilution; larger droplet populations indicate a coarse emulsion that may reduce the absorption rate. The gelatin shell is a structural weak point because ethanol and propylene glycol migrate from the fill into the gelatin matrix, plasticizing the shell and increasing the risk of seal failure, leakage, and capsule-to-capsule mass variation. The fill is deaerated under vacuum before encapsulation, and nitrogen blanketing is applied throughout mixing and storage to limit peroxide formation from the triglyceride phase. The shell is cast with a gel strength suitable for plasticizer migration, and filled capsules are dried at 20-25 °C and 30-40% RH until the shell moisture content determined by USP <921> Method Ia falls within the product-specific acceptance window. Packaging in cold-form aluminum-aluminum blisters with a desiccant sachet is used because PVC/PVDC blisters do not provide an adequate barrier against ethanol loss and moisture ingress. In-process controls include fill-mass uniformity, shell thickness, seal strength, and residual oxygen in the headspace. Release testing includes assay by USP <621>, dissolution by USP <711> Apparatus II, and water content by USP <921>. The dissolution medium for Ciclosporin capsules is typically an acidic medium with surfactant; the exact medium composition and paddle speed must be justified during method development because the microemulsion preconcentrate can release the drug so rapidly that a method without surfactant may fail to discriminate between acceptable and unacceptable batches.
Direct compression of crystalline Ciclosporin API is not feasible at production scale because the API has poor aqueous solubility, high lipophilicity, and poor flow from a hopper; the resultant tablets would show incomplete dissolution and high inter-tablet variability. A formulation route based on amorphous solid dispersion is required. Hot-melt extrusion on a co-rotating twin-screw extruder with an L/D 40:1 barrel and gravimetric feeding is one route; the API is blended with a polymer such as hypromellose acetate succinate or polyvinyl caprolactam-polyvinyl acetate-polyethylene glycol graft copolymer in a drug-to-polymer ratio of 1:1 to 1:5 w/w. The barrel temperature must remain above the glass transition temperature of the polymer to obtain a homogeneous melt, but below the degradation threshold of Ciclosporin; thermal excursions above 170 °C are avoided because degradation products of the cyclic peptide can appear under prolonged residence time. The melt is extruded through a die plate, cooled on a stainless-steel conveyor, milled, and then blended with microcrystalline cellulose, crospovidone, and sodium stearyl fumarate before compression on a rotary tablet press with precompression. Published data for specific Ciclosporin hot-melt extrusion formulations are limited; therefore the thermal behavior of the API-polymer dispersion should be verified by differential scanning calorimetry according to ASTM E1356 and thermogravimetric analysis according to ASTM E2550 during preformulation. The absence of a recrystallization exotherm in the milled extrudate after storage at 40 °C/75% RH for 1 month is a minimal stability indicator, while dissolution is tested using USP <711> Apparatus II with a surfactant-containing medium. Tablet hardness is controlled by USP <1217>, friability by USP <1216>, and uniformity of dosage units by USP <905>. Because the amorphous form is thermodynamically metastable, the operational boundary is narrow: excess moisture during compression can cause agglomeration; insufficient moisture can reduce tablet hardness due to poor bonding of milled dispersion particles. The compression environment is therefore maintained at 20-25 °C and 35-45% RH.
For single-dose sachets and granules that can be sprinkled onto soft food, fluid-bed granulation is selected when swallowing a capsule is not acceptable and dose fractionation at the bedside is required. The Ciclosporin API is first micronized or co-milled with a hydrophilic carrier to improve surface wetting, then dispersed in a binder solution, usually hypromellose E5 in purified water, and sprayed onto a fluidized bed of lactose monohydrate and pregelatinized starch in a top-spray fluid-bed processor. The granulation process window is narrow because the cyclic peptide is sensitive to hydrolytic degradation in the presence of free water at elevated temperature; therefore the inlet air temperature is maintained below 70 °C, the product temperature below 40 °C, and the final granule moisture content by USP <921> below 3.0% w/w. Binder concentration is held at 2-5% w/w of dry granulate, and the API content per sachet is adjusted by geometric dilution from 15 mg to 100 mg per dose. The dried granules are screened through a 1.0 mm sieve and filled into triple-layer aluminum sachets under low humidity. The terminal granule product must pass dissolution testing by USP <711> Apparatus III or Apparatus II, content uniformity by USP <905>, and loss on drying by USP <731>. Because granules are not a monolithic dosage form, the dissolution procedure must be adapted to account for the absence of compression; the use of a surfactant-containing medium is usually required to maintain sink conditions, and the method must be validated according to ICH Q2(R1) for linearity, accuracy, and precision. These granules are not interchangeable with reconstituted suspensions at the point of administration unless a documented equivalence study has been performed.
The injectable concentrate pathway centers on dissolution of Ciclosporin in a vehicle of polyoxyethylated castor oil and absolute ethanol under nitrogen, yielding a sterile concentrate at 50 mg/mL API. This vehicle is selected because Ciclosporin has negligible solubility in purely aqueous media; however, the surfactant fraction introduces a clinical risk of anaphylactoid reactions when the undiluted concentrate is administered rapidly. The concentrate must therefore be diluted with 0.9% sodium chloride injection or 5% dextrose injection to a final concentration of 0.5-2.5 mg/mL before intravenous infusion. Glass or polyolefin containers are specified for the admixture; PVC containers are not used because polyoxyethylated castor oil can extract di(2-ethylhexyl) phthalate from PVC tubing and bags, creating a leachable risk that is evaluated by USP <661.1> and ICH Q3C residual-solvent guidance. Filtration uses a sterilizing-grade 0.22 µm polyvinylidene fluoride membrane, and the fill-finish operation is performed by aseptic processing rather than terminal moist-heat sterilization because the cyclic peptide degrades at high temperature; sterility is confirmed by USP <71>, bacterial endotoxins by USP <85>, and particulate matter by USP <788>. An injectable-grade Ciclosporin API lot must meet a tighter bacterial endotoxin specification than oral-grade material; the exact limit is derived from the maximum dose and route of administration under USP <85> and is reported on the Certificate of Analysis. The dilution line is an additional processing step where pH shifts or insufficient mixing can cause precipitation of the peptide; the diluted admixture should be inspected visually for turbidity or particulate formation and should not be combined with other drugs in the same infusion container without documented compatibility. Published data for specific admixture stability are limited and should be generated on-site using HPLC assay by USP <621>; the stability window is not assigned as a universal value because it depends on container material, storage temperature, and admixture concentration.
When a ready-to-dispense oral liquid is required, the API is not simply suspended in water because of its low aqueous solubility and bitter taste; instead, a microemulsion preconcentrate is supplied as an oral solution to be diluted in milk, chocolate milk, or orange juice immediately before intake. The concentrate contains Ciclosporin at 100 mg/mL, corresponding to approximately 10% w/v API, in a vehicle of ethanol, medium-chain triglycerides, and a hydrophilic surfactant. The co-solvent fraction is sufficient to fully dissolve the API and prevent precipitation upon aqueous dilution; if ethanol content is too low, precipitation occurs in the dilution beverage; if too high, palatability and container compatibility issues increase. The concentrate is filled into amber glass bottles with a calibrated oral syringe to achieve dose accuracy; glass is used because ethanol permeability through plastic can reduce co-solvent content and shift phase behavior. The patient-specific dose is mixed with the beverage, and the microemulsion is stable enough for prompt administration, but the mixture should not be stored for extended periods because beverage components can alter droplet size and release kinetics. Quality tests include deliverable volume by USP <698>, assay by USP <621>, alcohol content by USP <611>, and microbial examination of nonsterile products by USP <61> and USP <62>. In-use stability after first opening must be justified, and the multidose container is assigned an in-use period based on microbial challenge data.
| Quality attribute | Method | Primary device or condition |
|---|---|---|
| Deliverable volume from oral solution | USP <698> | Calibrated oral syringe, 25 °C |
| Ethanol content | USP <611> | Gas chromatography with headspace injection |
| Assay and related substances | USP <621> | C18 reversed-phase HPLC, column 70 °C |
| Microbial examination | USP <61> and USP <62> | Nonsterile oral liquid acceptance criteria |
Competitive Ciclosporin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Ciclosporin Pharma Grade API is the isolated active pharmaceutical ingredient ciclosporin A, a cyclic undecapeptide calcineurin inhibitor with the molecular formula C62H111N11O12 and a theoretical molecular mass of 1202.61 g/mol. The substance is registered under CAS 59865-13-3 and is supplied as a white to almost-white powder for formulation into tablet, capsule, granule, oral solution, and injectable dosage forms. The grade designation separates oral-grade material from injection-grade material primarily on the basis of bioburden, bacterial endotoxin, residual solvent profile, and particulate control rather than molecular identity. Pharmacopoeial compliance is assessed against the current USP and Ph. Eur. monographs. Release testing includes HPLC assay under USP 621, related substances by gradient elution, water content by Karl Fischer titration under USP 921, residue on ignition under USP 281, and residual solvents under USP 467 with acceptance criteria aligned to ICH Q3C. The cyclosporin A content is typically specified as 98.0%–101.5% on the dried basis, with the exact range dependent on the monograph and manufacturer’s certificate of analysis. Unlike tacrolimus and sirolimus, which are macrolide-based small molecules, ciclosporin is a neutral hydrophobic cyclic peptide; its aqueous solubility is reported as less than 0.1 mg/mL at 25°C. Final dosage forms therefore require solubility enhancement, particle-size reduction, or emulsification rather than simple direct compression of crystalline drug alone.
| Parameter | Method or Standard | Typical Acceptance Criterion |
|---|---|---|
| Appearance | Visual inspection | White to almost-white powder |
| Identification | IR absorption; HPLC retention time | Matches reference standard |
| Assay, cyclosporin A | HPLC, USP 621 | 98.0%–101.5% on dried basis |
| Related substances | HPLC gradient | Specified impurities within monograph limits; total impurities not more than applicable monograph value |
| Water | Karl Fischer, USP 921 | ≤2.0% for oral grade; injection grade often ≤1.0% |
| Residue on ignition | USP 281 | ≤0.1% |
| Residual solvents | USP 467; ICH Q3C | Class 2 solvents within permitted daily exposure; Class 3 solvents within PDE |
| Bacterial endotoxins | USP 85; Ph. Eur. 2.6.14 | Calculated from injectable dose; oral grade may not require routine testing unless specified |
| Particle size distribution | Laser diffraction, USP 429 | d50 and d90 agreed between manufacturer and user; no universal monograph limit |
For low-dose tablet and capsule products containing 25 mg or less of ciclosporin per unit, content uniformity is the primary process risk. Milled ciclosporin exhibits cohesive, electrostatically charged particle behaviour that produces sticking to rotary tablet press tooling and segregation during bin-to-bin transfer. In V-blender trials, drug-rich fines tend to accumulate in the upper portion of the blend when the API is added directly to a full batch of microcrystalline cellulose; a two-stage mixing sequence using a tumble blender at 60% nominal vessel fill followed by screening through a 500 µm stainless-steel mesh reduces agglomerates but does not eliminate segregation. Roller compaction with ribbon milling is therefore preferred over wet granulation for heat-sensitive formulations because it avoids aqueous exposure and the associated polymorphic transition risk. Milled ribbon granules are generally denser and have a narrower particle size distribution than wet-massed granules, which improves die-fill consistency on a rotary tablet press operated at 30–50 rpm. API particle size is controlled by laser diffraction under USP 429; the d50 and d90 values are negotiated with the dosage-form developer because no universal compendial particle size specification exists. Published data for a single acceptable d90 across all oral dosage forms are limited. In direct compression, a preblend of API with approximately 25% of the filler is required before lubrication; blend uniformity by HPLC should show a relative standard deviation of ≤5.0% before magnesium stearate addition.
Fluid-bed top-spray granulation of ciclosporin-containing formulations is specified when the target product is a capsule or granule-filled sachet and direct compression is not feasible. The API is first dissolved or dispersed with a binder such as povidone or hypromellose in an aqueous-organic solvent system, then sprayed onto lactose monohydrate or microcrystalline cellulose cores in a Glatt GPCG-5 or equivalent fluid-bed unit. Inlet air temperature is maintained below the solvent flashpoint and the product bed temperature is held below 40°C to avoid thermal conversion of the partially amorphous API fraction. Granule moisture content is monitored by loss-on-drying and is typically terminated at 1.5%–2.5% water. End-process lubrication with magnesium stearate is limited to 0.5% w/w and mixed for 3–5 min to avoid over-lubrication, which lowers tablet hardness. The resulting granules are filled into hard gelatin or hypromellose capsules; capsule fill weight is monitored by in-process net fill weight, and dosage-unit uniformity is tested under USP 905.
Injection-grade ciclosporin API is distinguished from oral grades by mandatory bacterial endotoxin and bioburden specifications. Endotoxin is measured by Limulus amebocyte lysate kinetic chromogenic assay under Ph. Eur. 2.6.14 or USP 85, with the acceptance criterion calculated from the maximum injectable dose per kilogram of body weight. For parenteral products, the limit is derived as K/M, where K is 5 EU/kg/h for intravenous administration and M is the maximum bolus dose in milligrams per kilogram per hour. A bioburden limit of ≤100 CFU/g is commonly applied to the bulk API before sterile filtration; after sterile filtration and aseptic filling, the finished injection must meet sterility under USP 71 or Ph. Eur. 2.6.1. Residual solvent control is more restrictive than for oral grades because the injectable formulation frequently uses ethanol and polyoxyethylated castor oil to solubilise the cyclic peptide. Ethanol is controlled under ICH Q3C Class 3 limits, and any residual castor-oil-derived impurities are controlled by the API supplier. The API is typically dissolved in a solvent system containing dehydrated alcohol before further dilution in the final vehicle; this intermediate solution must be passed through a 0.22 µm sterilising-grade filter, and filter compatibility with ethanolic solutions must be established to avoid leachables.
Moist heat sterilisation is generally not used for ciclosporin injectable solutions because the API is susceptible to hydrolysis and thermal degradation; aseptic filtration with a sterilising-grade filter is the preferred route. On production lines, the concentrated ethanolic API solution is held in stainless-steel or glass-lined vessels; long hold times above 25°C are avoided because ethanol evaporative loss changes assay concentration. The final diluted concentrate is filtered through two serial 0.22 µm filters to reduce pre-filtration bioburden. Pre-use and post-use filter integrity testing is recorded according to ISO 13408-2; bubble point or water intrusion values are compared with the filter manufacturer’s minimum specification.
If a marketed oral dosage form relies on a microemulsion or a nanoparticulate intermediate, the API particle size, crystallinity, and emulsification characteristics become more critical than simple chemical purity. In a self-microemulsifying drug delivery system, ciclosporin is dissolved in a mixture of lipophilic phase, surfactant such as polysorbate 80 or Cremophor RH 40, and a co-solvent such as propylene glycol or ethanol. The resulting preconcentrate is expected to disperse in aqueous media to form droplets with a polydispersity index below 0.3 unless the approved product specification indicates otherwise. Laser diffraction and dynamic light scattering are used to measure droplet size distribution; the mean droplet diameter is formulation-specific, and published data for this specific API-formulation configuration are limited. For nanoparticulate granule-based products, high-pressure homogenisation at pressures between 500 bar and 1500 bar is employed, followed by spray drying or fluid-bed layering. X-ray powder diffraction under USP 941 is used to confirm the amorphous nature of the solid dispersion. Loss of crystallinity is not an impurity issue; rather, it is a deliberate process control for dissolution enhancement. In dissolution testing under USP 711, the dosage form is usually tested in water or simulated intestinal fluid with surfactants because the API’s solubility in plain water is insufficient for a sink condition. The FDA Dissolution Methods Database lists compendial dissolution methods for ciclosporin capsules; method conditions should be matched to the approved reference product or regulatory dossier.
Because ciclosporin is a cyclic undecapeptide, its physicochemical handling differs from that of tacrolimus, a macrolide lactone, and sirolimus, a macrocyclic lactone. The following table summarises API-level properties relevant to formulation. Molecular masses are average or monoisotopic as commonly cited; monograph values should be used for regulatory submissions.
| Property | Ciclosporin A | Tacrolimus | Sirolimus |
|---|---|---|---|
| CAS Registry Number | 59865-13-3 | 104987-11-3 | 53123-88-9 |
| Molecular formula | C62H111N11O12 | C44H69NO12 | C51H79NO13 |
| Molecular mass | 1202.61 g/mol | 804.018 g/mol | 914.172 g/mol |
| Structural class | Cyclic undecapeptide | Macrolide lactone | Macrocyclic lactone |
| Primary immunosuppressive mechanism | Calcineurin inhibition | Calcineurin inhibition | mTOR inhibition |
| Aqueous solubility | Practically insoluble; below 0.1 mg/mL | Practically insoluble | Practically insoluble |
| Oral formulation challenge | Low solubility; emulsification or solid dispersion | Low dose; content uniformity; humidity sensitivity | Low solubility; stabilised oral solution |
Bulk ciclosporin API should be stored in tight, light-resistant containers under refrigerated conditions, usually at 2–8°C unless the manufacturer’s stability data supports controlled room temperature. Oxygen and prolonged exposure to strong light should be avoided; the API is not classified as explosive, but fine powder can form a combustible dust cloud when dispersed in air. Process equipment should include dust extraction and bonding/grounding to control static discharge. The API is incompatible with strong oxidising agents; compatibility with acidic or basic excipients should be screened by high-performance liquid chromatography for degradation products before final formula selection. For injectable-grade material, opened containers should be handled in ISO-classified areas, and the residual material should be re-sealed under dry nitrogen to limit moisture uptake. Because ciclosporin is a narrow therapeutic index drug, batch-to-batch consistency of dissolution performance and impurity profile is normally verified against an approved reference standard rather than only against chemical assay.