| HS Code | 282111 |
| Product Name | CILOSTAN (Cilostazol) CR Tab. Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Brand Name | CILOSTAN |
| Active Ingredient | Cilostazol |
| Product Type | Pharma Grade API and controlled-release tablet |
| Dosage Forms | Tablet, capsule, granule, injection |
| Routes Of Administration | Oral and injectable |
| Cas Number | 73963-72-1 |
| Molecular Formula | C20H27N5O2 |
| Molecular Weight | 369.46 g/mol |
| Drug Class | Phosphodiesterase III inhibitor / antiplatelet agent / vasodilator |
| Mechanism Of Action | Increases cAMP by inhibiting PDE3, leading to platelet inhibition and vasodilation |
| Therapeutic Indication | Intermittent claudication |
| Contraindications | Congestive heart failure; hypersensitivity to cilostazol |
| Common Adverse Effects | Headache, diarrhea, dizziness, palpitations, peripheral edema |
| Warnings And Precautions | Avoid in heart failure; caution with CYP3A4 and CYP2C19 inhibitors; monitor bleeding and cardiovascular effects |
| Storage Conditions | Store at controlled room temperature 20-25°C (68-77°F); protect from light and moisture |
| Packaging | Pharma-grade API in sealed containers; finished dosage forms in blister packs or bottles |
| Shelf Life | Typically 24-36 months when stored as directed |
| Regulatory Status | Prescription-only medicine in many jurisdictions |
As an accredited CILOSTAN (Cilostazol) CR Tab. 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 | CILOSTAN (Cilostazol) CR pharma-grade API supplied in 25 kg double polyethylene-lined fiber drums, securely sealed for oral/injectable dosage manufacturing. |
| Container Loading (20′ FCL) | 20′ FCL loaded with CILOSTAN (Cilostazol) CR Tab/API, palletized, stretch-wrapped, secured, and shipped under pharma-grade, temperature-controlled conditions for oral/injectable use. |
| Shipping | CILOSTAN (Cilostazol) CR Tab. pharma-grade API is shipped in sealed, tamper-evident, moisture-barrier containers under controlled ambient conditions (15–25°C), protected from light and contamination. Each shipment includes COA, SDS, batch/lot documentation, and GMP-compliant labels. Comply with local transport, import, and pharmaceutical handling regulations. |
| Storage | Store CILOSTAN (Cilostazol) CR Tab Pharma Grade API in tightly closed, light-resistant containers in a cool, dry, well-ventilated area at controlled room temperature 20–25°C (68–77°F); excursions 15–30°C are permitted. Protect from moisture, heat, direct sunlight, and incompatible materials. Keep containers sealed and away from children. For oral/injectable grades, follow the manufacturer’s labeled storage requirements. |
| Shelf Life | Shelf life varies by dosage form; store cool, dry, protected from light. Typically tablets: 24–36 months; API: up to 60 months. |
The aqueous solubility of cilostazol at 25°C is documented in pharmacopoeial literature as below 1 µg/mL, which places the molecule within Biopharmaceutics Classification System Class II (low solubility, high permeability). This physicochemical profile drives every formulation decision in immediate-release tablet production. Without particle size reduction to a D90 ≤ 25 µm via air-jet micronization, dissolution rates fail to meet the acceptance criterion specified in USP <711> Apparatus II (paddle, 50 rpm, 900 mL 0.5% sodium lauryl sulfate) where Q = 80% within 30 min. Formulation addition ratio for the peripheral arterial disease indication is 100 mg API per tablet, representing 25–33% w/w of total tablet mass (300–400 mg target weight). Direct compression is not industrially viable due to poor flow and high compressibility demand; high-shear wet granulation is instead performed in a Gral 10 or Diosna P1-6 granulator with povidone K30 (3–5% w/w) as binder, croscarmellose sodium (2–4% w/w) as disintegrant, and magnesium stearate (0.5–1.0% w/w) as lubricant added in a terminal blending step. Granule moisture must be controlled to 2.0–3.5% w/w before compression on a Korsch XL 100 rotary press. Final tablet hardness is held at 80–120 N (per USP <1217>) with friability ≤ 1.0% (per USP <1216>). Impurity control follows ICH Q3A(R2) for the API (total impurities ≤ 0.5%, any unspecified individual ≤ 0.1%) and ICH Q3B(R2) for the drug product. Terminal products include 50 mg and 100 mg film-coated tablets for oral administration. Operational boundary: excipient pre-drying is mandatory when ambient relative humidity exceeds 60%; failure to control granule moisture produces picking and sticking on tooling within the first 30 min of compression, documented on production lines as a batch-to-batch variance that necessitates tooling polish and revalidation.
Although cilostazol exhibits an elimination half-life of 11–13 hours, the once-daily controlled-release matrix must sustain therapeutic plasma concentrations over a full 24-hour dosing interval. Hydrophilic matrix systems based on hypromellose (USP substitution type 2208, viscosity grade 100,000 mPa·s at 2% w/v in water) at 25–40% w/w of total tablet mass generate diffusion-erosion release profiles approximating zero-order kinetics over 18–22 hours when manufactured with controlled compression force. Tablets are produced on a rotary press equipped with pre-compression rollers set to 15–20 kN pre-compression and 150–200 kN main compression. Tablet hardness of 120–180 N is required to achieve the target release profile; over-compression above 200 N induces matrix densification that depresses release rates below acceptance criteria established in USP <711> extended-release methodology (Apparatus I at 100 rpm; 750 mL 0.1 N hydrochloric acid for 2 hours, then 250 mL phosphate buffer to pH 6.8, maintained at 37°C ± 0.5°C). Formulation addition ratio is 200 mg API per tablet; total tablet mass ranges 800–1000 mg, with release-modifying fillers (lactose monohydrate, microcrystalline cellulose PH 102) comprising 25–45% w/w. Direct compression of dry-blended API and hypromellose is feasible when API particle size D90 ≤ 15 µm; alternatively, roller compaction enhances flow for high-speed production. A non-functional film coating (Opadry II at 3% weight gain) is applied in a Glatt GC Master 750 perforated coating pan at inlet temperature 60–70°C, with product temperature maintained below 45°C to avoid structural collapse of the hypromellose gel layer. Stability protocols follow ICH Q1A(R2) at 25°C/60% RH long-term and 40°C/75% RH accelerated conditions. Content uniformity per USP <905> requires acceptance value AV ≤ 15. Terminal product is the extended-release tablet at 200 mg once-daily strength. Operational boundary: dissolution media containing greater than 0.5% sodium chloride depress gel layer formation and accelerate release non-biorelevantly; the ionic strength effect must be characterized during method transfer because it masks true formulation performance.For secondary prevention of non-cardioembolic ischemic stroke, cilostazol is administered at 100 mg BID in capsule dosage form across several Asian markets. Encapsulation presents fewer compressibility constraints than tableting but shifts quality risk toward granule flow, hygroscopicity, and content uniformity. The API is granulated via high-shear wet granulation (Gral 10, 5-L bowl, impeller 300 rpm, chopper 1500 rpm) with lactose monohydrate, corn starch, and povidone K25 (2–4% w/w) as binder; wet mass is dried in a fluid bed dryer (Glatt GPCG-1) to LOD 2.0–3.0% w/w, milled through a 0.8 mm screen (Comil 197S), and blended with magnesium stearate (0.5% w/w) and colloidal silicon dioxide (0.5% w/w). Addition ratio: 100 mg API per capsule; fill weight 280–350 mg depending on granule bulk density (target 0.45–0.55 g/mL). Encapsulation equipment includes IMA Zanasi 40E or Bosch GKF 1500 automatic capsule fillers, with dosing disc selection based on target fill weight and capsule shell size 2 or 3 (HPMC or gelatin). In-process controls specify granule particle size distribution D10 ≥ 50 µm, D90 ≤ 500 µm, and water activity ≤ 0.5 to suppress API degradation. Dissolution per Ph. Eur. 2.9.3 (paddle, 75 rpm, 900 mL 0.1 N HCl); content uniformity per Ph. Eur. 2.9.40 (AV ≤ 15); degradation products per ICH Q3B(R2); microbial limits per Ph. Eur. 5.1.4 (TAMC ≤ 10² CFU/g, TYMC ≤ 10¹ CFU/g). Terminal products are 50 mg and 100 mg hard gelatin or HPMC capsules. Limitation: capsule shell crosslinking is documented when residual aldehyde-containing excipient degradation products are present; avoid combination with povidone lots carrying measurable peroxide impurities above 400 ppm.
The injectable route for cilostazol addresses the clinical gap when oral administration is precluded, such as in patients with impaired swallowing or acute hemodynamic instability. However, aqueous solubility below 1 µg/mL renders conventional solution formulations impossible at clinically relevant doses without enabling strategies. Three approaches have industrial precedent: hydroxypropyl-β-cyclodextrin complexation, nanosuspension via high-pressure homogenization, and co-solvent systems with PEG 400 and propylene glycol. For nanosuspension, the API is dispersed in an aqueous vehicle containing poloxamer 188 (0.5–2.0% w/v) and polysorbate 80 (0.05–0.1% w/v) as steric and electrostatic stabilizers; the slurry is processed through a high-pressure homogenizer (Avestin EmulsiFlex-C3 or Stansted benchtop) at 100–200 MPa for 20–40 passes until particle size D50 ≤ 200 nm and D90 ≤ 500 nm measured by laser diffraction (Malvern Zetasizer Nano ZS). Addition ratio is typically 5–10 mg/mL API in nanosuspension; lyophilized product contains 50–100 mg per vial with cryoprotectant mannitol or trehalose (5–10% w/v). Aseptic processing per 21 CFR 211.113 and USP <1116> is mandatory because terminal sterilization is not feasible due to thermal sensitivity of cilostazol (degradation accelerates above 60°C). Sterile filtration (0.22 µm PVDF filter) is applied to the vehicle before aseptic mixing; lyophilization follows a cycle of freezing at -45°C, primary drying at -25°C for 24–36 hours, and secondary drying at 25°C for 6–8 hours.
| Test Parameter | Reference Standard | Acceptance Criterion |
|---|---|---|
| Sterility | USP <71> | No growth after 14 days incubation |
| Bacterial Endotoxins | USP <85> | ≤ 0.5 EU/mg (LAL method) |
| Particulate Matter (≥ 10 µm) | USP <788> | ≤ 6000 particles per container |
| Particulate Matter (≥ 25 µm) | USP <788> | ≤ 600 particles per container |
| Container Closure Integrity | USP <1> | No dye ingress after vacuum test |
| Stability (long-term) | ICH Q1A(R2) | 24-month shelf life at 25°C/60% RH |
| Aseptic Process Environmental Monitoring | 21 CFR 211.113, USP <1116> | Grade A: viable count 1 CFU/m³ |
Terminal products are lyophilized powders in Type I glass vials (5R or 10R) with bromobutyl rubber stoppers and aluminum overseals, reconstituted with sterile water for injection immediately prior to administration. Operational boundary: nanosuspension is thermodynamically metastable; Ostwald ripening produces particle growth within 24–48 hours post-reconstitution when stabilizer concentration falls below 0.5% w/v, which is a documented failure mode observed during early clinical batch stability testing. Published data for this specific injectable configuration is limited relative to oral dosage forms; formulation development must proceed under ICH Q8(R2) Quality by Design principles with iterative screening of stabilizer ratios.
In geriatric and dysphagic patient populations, tablet and capsule swallowing may be impossible or unsafe, necessitating granule dosage forms suitable for sprinkling on semi-solid food or dispersing in liquid. Granule manufacturing for cilostazol follows the wet granulation paradigm but imposes additional constraints on particle size distribution, taste-masking requirements, and dispersion kinetics. The granule blend is formulated with mannitol (25–35% w/w) as a rapidly dissolving filler, sucralose or xylitol (0.1–0.5% w/w) for bitter taste masking, sodium starch glycolate (2–4% w/w) as superdisintegrant, and povidone K30 (2–3% w/w) as binder. Granulation is performed in a fluid bed processor (Glatt GPCG-5) in top-spray mode at inlet temperature 55–65°C, spray rate 15–25 g/min, and atomizing pressure 1.5–2.5 bar. Addition ratio: 100 mg API per sachet; total granule mass 1.5–2.5 g per sachet, yielding API loading of 4–6.7% w/w. Particle size specification: all granules pass 850 µm sieve; ≥ 90% retained on 150 µm sieve (per JP 2.9.36), providing uniform dispersion without dust formation. Dissolution per JP 6.10 (paddle, 50 rpm, 900 mL water); content uniformity per JP 6.02; degradation products per ICH Q3B(R2); microbial limits per JP 4.01. Terminal products are sachet-filled granules in paper/aluminum/PE laminate, 100 mg per sachet. Operational boundary: granular formulations should be reconstituted in beverages at pH 5–7 and consumed within 30 minutes to avoid precipitation; combination with acidic liquids below pH 3 accelerates hydrolysis of the tetrazole ring and is contraindicated.
Fixed-dose combination tablets pairing cilostazol with acetylsalicylic acid or clopidogrel present a specific acid-base incompatibility: acetylsalicylic acid has pKa 3.5 while cilostazol is weakly basic with pKa 9.2, creating an interfacial microenvironment that accelerates degradation unless physical separation is maintained in bilayer architecture. A bilayer compression process using a rotary press (Korsch XM 12, first-layer pre-compression at 30 kN, main compression 80–120 kN for both layers) produces tablets where the cilostazol layer contains 100 mg API with microcrystalline cellulose, lactose monohydrate, croscarmellose sodium (2–3% w/w), and magnesium stearate (0.5% w/w), while the antiplatelet partner layer maintains its own excipient matrix. Addition ratio: cilostazol 100 mg plus acetylsalicylic acid 100 mg or clopidogrel 75 mg per tablet; total tablet mass 600–900 mg. Process criticality: layer-to-layer adhesion is the primary scale-up failure source. Insufficient first-layer compaction below 15 kN produces interlayer lamination during transfer from R&D (Fette 2200i, 40 stations) to pilot and production scales (Korsch XL 800, 65 stations). Magnesium stearate migration at the layer interface must be controlled by limiting over-lubrication to less than 5 minutes at 25 rpm in a Patterson-Kelley V-blender. Dual dissolution testing per USP <711> requires both APIs to achieve Q = 80% at 30 min in 0.1 N HCl. Stratified content uniformity per USP <905> addresses layer-to-layer API migration during storage. Impurity control per ICH Q3B(R2) includes salicylic acid (≤ 0.3% w/w relative to aspirin content) as a hydrolytic degradation marker and cilostazol-related unknowns. Terminal products are 100/100 mg and 100/75 mg bilayer film-coated tablets. Operational boundary: the acetylsalicylic acid-containing layer is hydrolytically unstable in presence of moisture; direct compression or roller compaction is mandatory, with granulation water content below 2.0% w/w and product temperature controlled at ≤ 25°C throughout manufacture to prevent aspirin degradation.In peripheral arterial disease intervention, drug-eluting stents coated with cilostazol have advanced to clinical evaluation, relying on the API's anti-restenotic activity via PDE3 inhibition in vascular smooth muscle cells. The coating process involves dissolution of cilostazol and a biodegradable polymer matrix, poly(D,L-lactic-co-glycolic acid) with lactide:glycolide ratio 50:50 and inherent viscosity 0.4–0.6 dL/g in hexafluoroisopropanol (HFIP), in an organic solvent system (chloroform, dichloromethane, or acetone) at an API:polymer mass ratio of 1:3 to 1:5, producing a coating solution with total solids concentration 2–5% w/v. The solution is applied to electropolished cobalt-chromium or nitinol stent platforms via ultrasonic spray coating (Sono-Tek MediCoat II) using 25–60 kHz nozzle atomizers at flow rate 0.2–1.0 mL/min, axial traverse speed 5–15 mm/s, and dry nitrogen flow at 10–20 L/min for solvent evaporation. Addition ratio: cilostazol loading 100–300 µg per stent; coating thickness 5–15 µm measured by scanning electron microscopy or optical profilometry; total drug content varies with stent diameter (6–12 mm for peripheral artery stents). Release kinetics: in vitro elution in phosphate-buffered saline pH 7.4 at 37°C exhibits biphasic behavior—initial burst release of 20–40% within 24 hours followed by sustained elution over 14–30 days, modulated by PLGA molecular weight and lactide:glycolide ratio. Standards include ISO 25539-2 for cardiovascular implants (endovascular devices), ASTM F2081-06 for drug-eluting stent characterization (drug content uniformity, coating integrity, particulate shedding), ISO 10993-5 for cytotoxicity, 21 CFR 820 for device quality management, and USP <71> for sterility of the final product via ethylene oxide or gamma sterilization at 25 kGy. Terminal products are balloon-expandable or self-expanding peripheral and coronary stents with cilostazol-eluting coating, 100–300 µg API per device. Operational boundary: cilostazol is sensitive to gamma radiation; API potency loss greater than 5% has been documented at doses above 25 kGy, requiring storage at -20°C during sterilization logistics and pre-sterilization overage calculations per ICH Q1B photostability guidance. Published data for this specific stent configuration is limited relative to oral dosage forms; coating process parameters must be validated per ASTM F2081-06 for each stent platform geometry and polymer lot.Competitive CILOSTAN (Cilostazol) CR Tab. Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.
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Designated as CILOSTAN (Cilostazol) CR Tab. Pharma Grade API, the product is supplied as a crystalline cilostazol base powder with a controlled particle-size distribution and pharmacopoeial-grade purity for use in oral solid dosage forms and, after additional bioburden and endotoxin controls, in injectable formulation development. Cilostazol is a selective phosphodiesterase III inhibitor; inhibition of cyclic adenosine monophosphate degradation in platelets and vascular smooth muscle produces antiplatelet and vasodilatory effects without clinically significant positive inotropy at the approved oral dose of 100 mg twice daily. The CR Tab. designation identifies a milled and sieved grade intended for controlled-release matrix tablets, capsules, and granules, with the base form rather than a salt or co-crystal. The API is tested against USP/NF and Ph.Eur. monographs, and batch release includes assay, related substances, residual solvents, elemental impurities, loss on drying, residue on ignition, particle size, bulk and tapped density, and X-ray powder diffraction. The product is packaged in double low-density polyethylene bags inside a fiber drum containing desiccant and is assigned a retest period of 36 months when stored below 25 °C and 60% relative humidity. The as-supplied API is non-sterile and is not terminally sterilized; injectable manufacturing sites must apply subsequent sterile filtration, aseptic processing, or terminal sterilization after formulation.
Direct compression of CILOSTAN (Cilostazol) CR Tab. Pharma Grade API on a rotary tablet press with B-tooling operated at 40–80 rpm requires defined particle-size and flow inputs. The particle-size distribution is controlled to D50 15–30 µm and D90 ≤45 µm by laser diffraction on a Malvern Mastersizer 3000 with dry dispersion at 1 bar. Bulk density is held at 0.35–0.55 g/mL and tapped density at 0.45–0.65 g/mL by USP <616> Method I and II. These inputs support a Carr index of 15–22 and a Hausner ratio of 1.10–1.30, which reduce die-fill variability without wet granulation. In a representative direct-compression matrix containing microcrystalline cellulose PH-102, lactose monohydrate 100 mesh, pregelatinized starch, croscarmellose sodium, and magnesium stearate, the API is pre-blended for 10 min at 15 rpm in a bin blender; magnesium stearate is added at 0.5–1.0 wt% and mixed for 3 min to avoid over-lubrication. Compression force between 8 kN and 15 kN produces tablets with hardness 60–100 N and friability below 1.0% when tested according to USP <1216>. Content uniformity at 20–30 kg batch scale meets USP <905> acceptance criteria when the API is not exposed to relative humidity above 60% during hopper residence. In transfer runs on a 19-station rotary press, batch-to-batch variance in tablet hardness remained within ±5 N when the API D90 was held below 45 µm. The controlled-release matrix performance depends on the hydrophilic polymer grade; in hypromellose matrices, the release profile is qualified by USP <711> Apparatus II at 50 rpm in 900 mL of pH 6.8 phosphate buffer, with acceptance criteria set by the finished-product marketing authorization and not by the API alone.
For oral capsule and granule operations, the CR Tab. grade is compatible with roller compaction and high-shear wet granulation. Roller compaction on a Gerteis Mini-Pactor at roll force 4–8 kN/cm and gap 1–2 mm yields ribbons with density 0.9–1.1 g/cm³; subsequent milling through a 0.8 mm screen produces granules suitable for capsule filling on an MG2 Planeta or equivalent dosator machine. Granulation with water or an aqueous binder solution requires the API to be pre-dried at 40 °C for 2 h if loss on drying exceeds 0.5%, because residual moisture above 0.8% promotes agglomeration and retards dissolution in hypromellose-based matrices. Capsule filling of the API without granulation is limited by its low bulk density and cohesive fines; if capsule filling is attempted, a minimum of 25–30% diluent premix by weight is recommended to maintain fill-weight uniformity.
Release of CILOSTAN (Cilostazol) CR Tab. Pharma Grade API is controlled under ICH Q7 and EU GMP Part II. The following specification profile applies to the oral grade; injectable-grade material adds the endotoxin and particulate controls listed separately.
| Parameter | Acceptance Criterion | Method / Standard |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual |
| Identification | Infrared absorption spectrum consistent with reference | USP <197>, Ph.Eur. 2.2.24 |
| Assay on dried basis | 98.0–102.0% w/w | USP <621> HPLC |
| Total related substances | ≤0.5% | Validated HPLC, ICH Q2 |
| Loss on drying | ≤0.5% | USP <731> |
| Residue on ignition | ≤0.1% | USP <281> |
| Elemental impurities | Per ICH Q3D | USP <232>, <233> |
| Residual solvents | Per USP <467> and ICH Q3C | Headspace GC |
| Particle size | D50 15–30 µm; D90 ≤45 µm | Laser diffraction, Malvern Mastersizer 3000 |
| Bulk density | 0.35–0.55 g/mL | USP <616> Method I |
| Tapped density | 0.45–0.65 g/mL | USP <616> Method II |
| Polymorph | X-ray powder diffraction pattern consistent | Ph.Eur. 2.9.33 |
| Microbial limits | TAMC ≤100 CFU/g; TYMC ≤10 CFU/g | USP <61>, <62> |
| Bacterial endotoxins, injectable screening | <0.5 EU/mg | USP <85> |
When an injectable presentation is developed, transfer of the API from oral grade to injection grade introduces controls not required for solid oral dosage forms. The base has aqueous solubility below 0.01 mg/mL at 25 °C; therefore a solubilizing system containing a cyclodextrin derivative, a co-solvent such as polyethylene glycol 300 or propylene glycol, or a lipid emulsion is needed before sterile filtration. The API as supplied is non-sterile; the formulated product must be passed through a sterilizing-grade filter, typically 0.22 µm polyvinylidene fluoride or polyethersulfone, and filled aseptically. Pre-filtration bioburden should be controlled below 10 CFU/100 mL to comply with current EU GMP Annex 1 expectations. Bacterial endotoxin limits for the API are set at <0.5 EU/mg when the material is intended for parenteral screening, but finished-product endotoxin limits must be justified by the maximum daily dose and route. Particulate matter in the finished injection is tested according to USP <788> or Ph.Eur. 2.9.19; visible and subvisible particle counts are formulation-dependent. Because terminal sterilization by moist heat may alter the polymorph stability and dissolution behavior of cilostazol, the preferred manufacturing route is aseptic filtration of a solubilized form; published data on terminal sterilization of this specific injectable configuration is limited.
If terminal sterilization of a CILOSTAN (Cilostazol) CR Tab. Pharma Grade API-containing parenteral product is considered, the thermal exposure should be limited to 121 °C for 15 min only after confirming that the formulation does not show polymorphic conversion or release of the API from the drug product matrix. Cilostazol base has a melting point near 159–160 °C; however, exposure to moist heat in the presence of water can accelerate hydrolysis of the amide bond and generate related substances that are controlled at ≤0.5% in the oral API specification. Steam sterilization of dry API powder is not recommended because the bulk powder may be heat-labile and surface moisture can cause caking and changes in particle-size distribution. If terminal sterilization is unavoidable, the formulated solution should be sparged with nitrogen and the headspace oxygen content maintained below 2% to reduce oxidative degradation. Sterilization validation would require demonstration of a sterility assurance level of 10-6 according to ISO 14937 or USP <1229>, with endotoxin and particulate limits reconfirmed after the sterilization cycle.
Compared with conventional unmilled cilostazol API, CILOSTAN (Cilostazol) CR Tab. Pharma Grade API reduces segregation in low-dose direct-compression blends. A conventional API lot may exhibit a broad particle-size distribution with D50 values between 40 µm and 100 µm and D90 values above 200 µm, which increases the risk of content uniformity failures under high-speed compression above 60 rpm. The CR Tab. grade maintains a tight span of 1.5–2.5 and removes oversize particles through a 325 mesh or 45 µm sieve, improving batch-to-batch consistency. Unlike a simple micronized powder, which may improve dissolution but worsen flow and increase electrostatic adhesion, the CR Tab. grade balances size reduction with bulk density to maintain die-fill consistency. Against other PDE3 inhibitor APIs such as milrinone and inamrinone, cilostazol base offers a distinct pharmacological profile: antiplatelet and vasodilatory activity with lower risk of positive inotropy at the approved dose. The controlled-release tablet grade is not a salt, so pH-dependent solubility must be considered in matrix selection; enteric or pH-modifying excipients may be required if the formulation targets pH-independent release. Published data for the comparative tableting performance of this specific grade against other suppliers’ cilostazol APIs is limited; the following representative preformulation data illustrate the observed differences.
| Parameter | CILOSTAN CR Tab. API | Conventional unmilled cilostazol API | Manufacturing significance |
|---|---|---|---|
| D50 | 15–30 µm | 40–100 µm typical | Low-dose uniformity |
| D90 | ≤45 µm | up to 250 µm typical | Reduced segregation |
| Span (D90−D10)/D50 | 1.5–2.5 | 3.0–5.0 typical | Die-fill consistency |
| Bulk density | 0.35–0.55 g/mL | 0.25–0.40 g/mL typical | Direct-compression feasibility |
| Content uniformity RSD, low-dose blend | ≤4% | 6–10% reported range | USP <905> acceptance |
| Residual particles >45 µm | ≤5% | 20–40% typical | High-speed compression |
For warehousing and dispensing, the API should be handled according to ICH Q1A and the supplier’s retest statement. The material is stored in double polyethylene bags with desiccant at or below 25 °C and 60% relative humidity. Prolonged exposure to relative humidity above 60% during hopper residence should be avoided because caking can increase particle agglomeration and require re-milling. Contact with strong oxidizing agents and highly acidic or alkaline aqueous media should be avoided during formulation, because cilostazol base undergoes pH-dependent degradation. Wet granulation contact surfaces should be stainless steel 316L or higher; uncoated steel surfaces are not recommended. The as-supplied API is not sterile and must be handled as a chemical intermediate under local occupational exposure limits.