| HS Code | 730491 |
| Productname | Glimepiride Micronized IP/USP/EP/BP Pharma Grade API |
| Synonym | Glimepiride |
| Casnumber | 93479-97-1 |
| Molecularformula | C24H34N4O5S |
| Molecularweight | 490.62 g/mol |
| Chemicalname | 3-ethyl-4-methyl-N-[2-[4-[(4-methylcyclohexyl)carbamoylsulfamoyl]phenyl]ethyl]-2-oxo-5H-pyrrole-1-carboxamide |
| Drugclass | Sulfonylurea antidiabetic |
| Grade | Pharma Grade API |
| Pharmacopoeia | IP/USP/EP/BP |
| Appearance | White or almost white crystalline powder |
| Micronizedform | Micronized; typically D90 ≤ 10 µm |
| Solubility | Practically insoluble in water; soluble in dimethylformamide; slightly soluble in methanol |
| Meltingpoint | 207°C |
| Storage | Store in a cool, dry, well-ventilated area, protected from light and moisture |
| Purity | ≥ 99.0% |
| Dosageforms | Tablet, Capsule, Granule, Injection |
| Routeofadministration | Oral and Injectable |
| Usage | Treatment of type 2 diabetes mellitus |
| Packaging | Foil bag inside fiber drum |
| Shelflife | 2-3 years when stored properly |
As an accredited GLIMEPIRIDE Micronized IP/USP/EP/BP 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 | Glimepiride Micronized IP/USP/EP/BP API is packed in 1 kg double-lined polyethylene bags inside sealed fiber drums for pharmaceutical manufacturing. |
| Container Loading (20′ FCL) | 20′ FCL: palletized, sealed drums of micronized Glimepiride IP/USP/EP/BP pharma-grade API, securely strapped, clean, dry, for global shipment. |
| Shipping | Glimepiride Micronized IP/USP/EP/BP API is shipped in sealed, light-resistant, double LDPE-lined fiber drums under controlled ambient conditions, protected from moisture, heat, and light. Air/sea freight includes MSDS, COA, and packing list; non-hazardous, cGMP-compliant handling for oral and injectable pharmaceutical use. Appropriate labels, tamper-evident closures, and temperature monitoring where required. |
| Storage | Store Glimepiride Micronized API in tightly closed, light-resistant containers within a cool, dry, well-ventilated, GMP-compliant area. Maintain controlled room temperature 15–30°C; protect from moisture, humidity fluctuations, and direct sunlight. Keep away from oxidizers, incompatible materials, and cross-contamination. Segregate oral and injectable grades. Store in original packaging, do not freeze, and follow label, SDS, and local regulations. |
| Shelf Life | Shelf life is typically 2–3 years in original, tightly sealed packaging, protected from light and moisture at controlled room temperature. |
Micronised glimepiride is incorporated into immediate-release tablet cores at 1–4% w/w relative to a core mass of 80–120 mg; at the 1 mg strength, the API fraction approaches 1.0% w/w, below which stratified sampling under USP <905> demonstrates content uniformity drift in direct compression blends. The commercial process therefore divides into two routes: direct compression is restricted to small batches where the micronised API is pre-dispersed by geometric trituration through a 300 µm stainless steel screen, and high-shear wet granulation is used for routine scale-up. In high-shear wet granulation, the API is combined with lactose monohydrate and microcrystalline cellulose in a top-drive granulator with impeller tip speed 2.5–6.0 m/s; purified water is sprayed until granulate moisture measured by loss-on-drying at 85 °C reaches 1.5–2.5%. The wet mass is milled through a 1.0 mm screen, dried in a fluid-bed dryer with inlet air at 55–65 °C, and dry-milled. Sodium starch glycolate (2.0–4.0% w/w) and magnesium stearate (0.5–1.0% w/w) are added extragranularly; the final blend is compressed on a rotary press with precompression 4–7 kN and main compression 8–14 kN, giving hardness 40–70 N and friability below 0.8%. Dissolution is assessed by USP <711> Apparatus II at 75 rpm in 900 mL of phosphate buffer pH 7.8, and content uniformity by USP <905>. Compliance anchors are ICH Q3A for process impurities, ICH Q3D for elemental impurities, ICH Q6A for specifications, and 21 CFR 211.110 for in-process sampling. Terminal product types are film-coated immediate-release tablets of 1 mg, 2 mg, 3 mg, and 4 mg.
| Component role | Representative excipient | Range (% w/w) | Process function |
|---|---|---|---|
| Drug substance | Micronised glimepiride IP/USP/EP/BP | 1.0–4.0 | Sulfonylurea active |
| Diluent | Lactose monohydrate | 35.0–60.0 | Brittle filler with aqueous solubility |
| Diluent/binder | Microcrystalline cellulose | 20.0–40.0 | Plastic compressibility |
| Disintegrant | Sodium starch glycolate | 2.0–4.0 | Capillary wicking |
| Lubricant | Magnesium stearate | 0.5–1.0 | Die ejection |
Bilayer fixed-dose combination tablets place micronised glimepiride in a low-mass layer (80–150 mg) laminated onto a metformin HCl layer (500–1000 mg). The glimepiride addition ratio is 0.1–0.3% w/w of the total bilayer mass at 1–4 mg per unit, while the glimepiride layer itself contains 1.0–5.0% w/w API. The critical process parameter is compression force partitioning: the first layer is precompressed at 4–8 kN to create a defined interface, after which the second layer is compressed at 12–20 kN; insufficient precompression leads to delamination at the interface, while excessive precompression prevents interlayer bonding and produces capping during coating. Rotary bilayer presses with 45 kN or 60 kN main compression capability and vacuum-assisted die filling are used because the metformin layer has poor flow and high bulk volume. In-process controls include weight, hardness, and layer thickness by near-infrared spectroscopy; content uniformity is tested under USP <905> with stratified sampling across the compression run. Dissolution uses USP <711> Apparatus II at 75 rpm in 900 mL of the pH 7.8 phosphate buffer for glimepiride and a separate metformin medium from its monograph. Compliance includes ICH Q3B for degradation products and 21 CFR 211.84 for incoming API identity and micronisation. Terminal products are bilayer tablets containing 1 mg/500 mg, 2 mg/500 mg, 1 mg/1000 mg, and 2 mg/1000 mg glimepiride/metformin HCl.
For low-dose clinical trial supply, micronised glimepiride is filled into hard gelatin capsules by geometric dilution with lactose monohydrate and pregelatinised starch. The API fraction is constrained to 0.3–2.0% w/w because capsule fill weight in size 3 capsules is typically 120–180 mg and the unit dose is 0.5–4 mg; below 0.3% w/w, static adhesion of micronised API to the drum surface of a tumble blender causes assay loss. The blend is prepared in an intensifier-bar tumble blender at 60–70% nominal volume, with a drug pre-blend passed through a 250 µm screen before addition to the main diluent. Capsule filling is performed on a dosator machine with dosing chamber vacuum; tamping-pin machines are generally less suitable for this low-API fraction because the pins compact the blend and alter dissolution. In-process monitoring includes fill weight at 10–15 minute intervals and content uniformity of filled capsules by USP <905>. Dissolution is tested with USP <711> Apparatus II at 75 rpm using a sinker specified in the capsule monograph, because hard gelatin shells may float. Compliance anchors are 21 CFR 211.84 for excipient acceptance, ICH Q3C for residual solvents in the granulation step, and Ph. Eur. 2.9.5 for uniformity of mass of single-dose preparations. Terminal product types are size 3 hard gelatin capsules of 0.5 mg, 1 mg, 2 mg, and 4 mg for blinded dose-ranging studies.
Single-dose sachets of glimepiride granules require particle size distribution control to prevent segregation of micronised API. The formulation uses mannitol as a water-soluble diluent, pregelatinised starch as binder, and hypromellose as a wetting agent; the API addition ratio is 0.1–0.5% w/w because a 1 g sachet containing 1–4 mg API yields an extremely dilute active phase. Wet granulation is carried out in a fluid-bed granulator with inlet air temperature 50–60 °C, spraying a 5–8% w/w aqueous binder solution at 20–40 g/min; the endpoint is determined by outlet air temperature and droplet size, not by absolute moisture alone, to limit over-wetting of the mannitol matrix. Granules are sieved to retain 125–500 µm particles; fines below 125 µm are recycled into the granulation liquid only after milling, because direct recycle of micronised API-rich fines produces superpotent clusters. Terminal heat-sealed sachets are filled on vertical form-fill-seal equipment with a vibratory feed; fill weight is maintained at RSD ≤1.5%. Quality standards are Ph. Eur. 2.9.1 for disintegration, USP <711> for dissolution, and ICH Q1A for stability. Terminal products are 1 g sachets delivering 1 mg, 2 mg, or 4 mg glimepiride.
Orodispersible tablets containing micronised glimepiride use two distinct process routes. In freeze-dried forms, a suspension of API, gelatin or fish collagen, mannitol, and purified water is dispensed into preformed blister wells, frozen at −40 °C, and lyophilised; the resulting matrix has high porosity and disintegrates in 3–10 s in the oral cavity but is moisture-sensitive and requires aluminium-aluminium blister protection. The API addition ratio in the final dried matrix is 0.7–5.0% w/w because the lyophilised unit mass is only 80–150 mg. In high-speed direct compression, the ratio is 0.5–2.0% w/w, with crospovidone (5–10% w/w) and mannitol-based coprocessed filler; the blend is compressed on a 27-station rotary press at 8–12 kN to produce tablets with hardness 25–40 N. Process conflicts arise when superdisintegrant swelling competes with adequate mechanical strength, so tablet hardness is monitored as a range rather than a single point. Disintegration is tested by Ph. Eur. 2.9.1 or USP <701>; dissolution follows USP <711> Apparatus II at 75 rpm in 500 mL of pH 6.8 buffer. Compliance includes ICH Q3D for elemental impurities from polymerisation residues and 21 CFR 211.67 for lyophiliser sterilisation. Terminal products are 1 mg and 2 mg orodispersible tablets for use without water.
Aseptic processing of micronised glimepiride for parenteral administration is limited to investigational drug product for pre-clinical toxicology and Phase I bioavailability studies; no approved injectable dosage form is listed in the major pharmacopoeias for this sulfonylurea. The formulation uses a sterile aqueous vehicle with pH adjustment because glimepiride aqueous solubility is low; typical API loading is below 1.0 mg/mL when prepared as a wet-media milled nanosuspension, with particle size controlled to D90 ≤500 nm by high-pressure homogenisation at 15,000–20,000 psi. Published data for specific clinical injectable configurations is limited, and batch composition is protocol-driven rather than harmonised. Aseptic filtration of the saturated solution can be used only after the vehicle is filtered, but the suspension itself cannot be sterilised by terminal filtration; the components are sterilised separately, and the final suspension is compounded under unidirectional airflow in an ISO 5 environment. The production process requires a media mill with yttrium-stabilised zirconium oxide beads of 0.1–0.3 mm, followed by vial filling under isolator conditions. Compliance anchors are EU GMP Annex 1, 21 CFR 210/211, ICH Q3C for solvent residues, and USP <789> for particulate matter in injections. Terminal product types are sterile investigational vials of 0.5 mg/5 mL to 2 mg/5 mL nominal concentration.
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The multicompendial API designated GLIMEPIRIDE Micronized IP/USP/EP/BP Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is released against current monographs of the Indian Pharmacopoeia, United States Pharmacopeia, European Pharmacopoeia, and British Pharmacopoeia. The API is identified chemically as glimepiride, CAS 93479-97-1, with molecular formula C24H34N4O5S and molecular weight 490.62 g/mol. Micronization is applied to reduce primary particle size for dissolution-limited absorption, because glimepiride behaves as a low-aqueous-solubility, weakly acidic sulfonylurea with pH-dependent dissolution. The grade is intended for dry blending, wet or dry granulation, capsule filling, and direct compression. If an injectable presentation is pursued, the API is not designated sterile by the manufacturer and must undergo further processing to meet parenteral requirements. Compared with unmicronized powder of the same chemical entity, the micronized material shows a larger specific surface area, lower bulk density, and greater electrostatic charge retention. These properties require process controls during dispensing, sieving, and blending to avoid segregation, dusting, and loss of blend uniformity. Polymorphic identity is controlled by X-ray powder diffraction against the current compendial reference standard, and residual solvent content is controlled according to ICH Q3C with the methods of USP <467> and Ph. Eur. 5.4.
Identity is confirmed by infrared absorption spectrophotometry and by retention time agreement in the liquid chromatographic assay. The assay acceptance range in current monographs is generally 98.0–102.0% on the dried basis; a multicompendial release protocol may apply a tighter manufacturer range of 99.0–101.0% to ensure that every lot remains within all four pharmacopoeial limits. Related substances are determined by HPLC under the conditions of USP <621> and Ph. Eur. 2.2.29; typical control thresholds limit individual specified impurities to not more than 0.10% and total impurities to not more than 0.5%, although the current monograph should be consulted for compound-specific impurity factors. Loss on drying is measured by USP <731> or Ph. Eur. 2.2.32, and water content by USP <921> or Ph. Eur. 2.5.12. Sulfated ash is controlled by USP <281> or Ph. Eur. 2.4.14. Residual solvents are limited to the class 2 and class 3 options of ICH Q3C, with benzene, carbon tetrachloride, and 1,2-dichloroethane typically excluded or controlled at the parts per million limits given in the relevant monograph. Elemental impurities are controlled under USP <232>, Ph. Eur. 5.20, and ICH Q3D.
| Attribute | Pharmacopoeial method | Typical release limit |
|---|---|---|
| Assay on dried basis | USP <621>, Ph. Eur. 2.2.29 | 98.0–102.0% |
| Related substances | USP <621>, Ph. Eur. 2.2.29 | Individual ≤0.10%; total ≤0.5% |
| Residual solvents | USP <467>, Ph. Eur. 5.4 | ICH Q3C class limits |
| Particle size distribution, micronized grade | USP <429>, Ph. Eur. 2.9.31 | D90 ≤10 µm |
| Bulk and tapped density | USP <616>, Ph. Eur. 2.9.34 | Report result |
| Water content | USP <921>, Ph. Eur. 2.5.12 | ≤0.5% or monograph limit |
| Sulfated ash | USP <281>, Ph. Eur. 2.4.14 | ≤0.1% |
In low-dose solid oral dosage forms containing 1 mg, 2 mg, 3 mg, 4 mg, 6 mg, or 8 mg of glimepiride per unit, the API fraction is often below 5% of total tablet weight. At this concentration, the critical process risk is not chemical degradation but physical segregation and poor content uniformity. Micronized glimepiride adheres to blender surfaces and charge-sensitive excipients. On a 600 L bin blender, colloidal silicon dioxide at 0.1–0.5% and a blending time of 15–25 minutes reduce electrostatic agglomeration but can increase the risk of over-lubrication if magnesium stearate is added too early. Content uniformity is assessed by USP <905> or Ph. Eur. 2.9.40; for low-dose tablets, acceptance values below 15 are generally required for the finished dosage form. Segregation during compression is minimised by matching the particle size distribution of the glimepiride with that of the filler, typically lactose monohydrate or dibasic calcium phosphate dihydrate.
Micronized glimepiride with a laser diffraction D90 of 10 µm or less does not necessarily retain that distribution after wet granulation. In high-shear mixers operating with an impeller tip speed of 5–10 m/s and a chopper speed of 1500–3000 rpm, binder addition rate determines agglomerate size. Rapid addition of aqueous binder can produce wet agglomerates above 500 µm, while slow addition with high chopper speed may generate granules with a D50 of 80–150 µm after wet milling and drying. The performance of the final tablet is governed less by the API particle size after granulation than by granule porosity, binder type, and the extent of glimepiride dissolution within the granule liquid bridges. Dissolution testing according to USP <711> or Ph. Eur. 2.9.3 should be used to confirm that the granulation route does not retard release in the chosen medium. For hydrophobic glimepiride, sodium lauryl sulfate at 0.1–0.5% in the dissolution medium or formulation may be required to obtain discriminatory release data.
The sulfonylurea group in glimepiride is susceptible to hydrolytic cleavage under acidic and strongly alkaline conditions, and this risk increases when aqueous granulation is performed above 60 °C. Aqueous granulation is therefore avoided or strictly controlled in formulation development. Non-aqueous granulation with ethanol or isopropanol, or dry granulation by roller compaction, is preferred when related substances rise above 0.2% during wet massing. Drying after aqueous granulation should achieve a final granule moisture content below 2.0%, with inlet air temperature in a fluid-bed dryer held between 50 °C and 60 °C and exhaust temperature monitored at 30–35 °C. Batch-to-batch variation in related substances can be attributed to residual water in the granule rather than to API instability alone; therefore, the drying endpoint should be correlated with loss on drying by USP <731> or Ph. Eur. 2.2.32 and not solely with exhaust temperature. When roller compaction is used, ribbon density is controlled between 0.9 g/cm³ and 1.1 g/cm³, and the milled granule is screened through an 800 µm sieve to prevent oversized granules from causing weight variation.
The term injectable does not correspond to a dedicated sterile grade in current glimepiride monographs. A formulation intended for parenteral administration must be prepared from the same multicompendial API but must additionally meet the end-product requirements for sterility, bacterial endotoxins, particulate matter, and container closure integrity. Sterility testing is performed under USP <71> or Ph. Eur. 2.6.1. Bacterial endotoxins are controlled by USP <85> or Ph. Eur. 2.6.14, with a limit that is dose-dependent and typically not above 0.5 EU/mg for parenteral products. Particulate matter in the finished injection is assessed by USP <788> or Ph. Eur. 2.9.19; the micronized API itself is not expected to meet these limits before terminal sterilisation or aseptic compounding. Because glimepiride exhibits low aqueous solubility at neutral pH, injectable formulation work generally requires pH adjustment above 7.5, co-solvent addition, or complexation. Published data for this specific configuration is limited, and each formulation must be validated for chemical and physical stability under ICH Q1A storage conditions.
Direct compression of micronized glimepiride is possible only when the API is first ordered mixed with a suitable carrier to reduce the cohesive forces created by high surface area. The flow function coefficient of the API is low. Bulk density and tapped density measured by USP <616> or Ph. Eur. 2.9.34 typically show a Carr index above 30, indicating poor flow and the need for a glidant. Roller compaction is often used instead of direct compression because it converts low-density micronized powder into dense ribbons and then into granules with improved flow. The main failure mode on tablet presses is sticking to punch faces when granule moisture exceeds 2.5% or when lubricant level is below 0.5%. Magnesium stearate at 0.5–1.0% reduces ejection force, but excessive mixing time with magnesium stearate can retard dissolution of low-solubility glimepiride. The lubricated blend is typically mixed for 3–5 minutes after the final excipient addition, and tablet hardness is monitored to remain within 40–80 N for immediate-release formulations to avoid disintegration delay. Disintegration is assessed by USP <701> or Ph. Eur. 2.9.1, and dissolution is assessed by USP <711> or Ph. Eur. 2.9.3.
Compared with unmicronized glimepiride, the micronized multicompendial grade presents a narrower particle size distribution by laser diffraction and a larger specific surface area, which can increase dissolution rate but also increases sensitivity to moisture and electrostatic charge. A single-compendial grade may be acceptable for a given market, but the multicompendial release protocol eliminates the need for separate qualification when submissions span jurisdictions recognising IP, USP, EP, or BP monographs. Differences from other sulfonylurea APIs such as glibenclamide or gliclazide are primarily pharmacological and formulational: glimepiride is used at lower unit doses and is often formulated with a low API fraction, whereas higher-dose sulfonylureas present different blend uniformity and dissolution challenges. The micronized product is not a co-processed excipient system; it is the pure API with particle size reduction and compendial compliance, and it does not provide built-in stabilisation against hydrolysis or electrostatic charging. Any downstream formulation using this API must therefore be developed with the same process controls as would apply to any micronized, low-solubility, dissolution-limited active substance.