| HS Code | 494784 |
| Api Name | Ceftazidime (Sterile) Pharma Grade API |
| Drug Classification | Third-generation cephalosporin antibiotic |
| Cas Number | 72558-82-8 |
| Chemical Formula | C22H22N6O7S2 |
| Molecular Weight | 546.58 g/mol |
| Physical Appearance | White to off-white crystalline powder |
| Solubility | Slightly soluble in water; soluble in dilute acidic and alkaline solutions |
| Purity Assay | 98.0% to 101.0% on dried basis |
| Grade | Pharma Grade API |
| Sterility | Sterile and pyrogen-free |
| Intended Dosage Forms | Tablet, Capsule, Granule, and Injection |
| Administration Routes | Oral and Injectable |
| Storage Conditions | Store below 25°C in a tightly sealed container, protected from light |
| Mechanism Of Action | Inhibits bacterial cell wall synthesis by binding to penicillin-binding proteins |
| Therapeutic Use | Treatment of serious bacterial infections including those caused by Pseudomonas aeruginosa |
| Microbiological Scope | Broad-spectrum activity against Gram-negative and Gram-positive bacteria |
As an accredited Ceftazidime (sterile) 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 | Sterile Ceftazidime API supplied in sealed drums, double polyethylene-lined, 10 kg net each, with certificate of analysis. |
| Container Loading (20′ FCL) | 20′ FCL loaded with sterile Ceftazidime Pharma Grade API in sealed containers, ready for oral and injectable pharmaceutical manufacturing. |
| Shipping | Shipping: Sterile Ceftazidime API is packed in airtight, light-protected, moisture-resistant pharmaceutical-grade containers. Ship under controlled temperature (2–8°C) using insulated cartons with gel packs/dry ice as required. Ensure tamper-proof sealing, clear hazard labeling, and include COA and stability documentation for oral and injectable use. |
| Storage | Store Ceftazidime sterile API in its original tightly closed container, protected from light, in a cool, dry place. Recommended storage: 20–25°C (controlled room temperature), avoiding excessive heat and moisture. Ensure container remains sealed to preserve sterility and stability. Do not freeze. Handle with care to maintain integrity for oral and injectable formulations. |
| Shelf Life | Shelf life: 24 months from manufacture when stored at controlled room temperature, protected from light and moisture, in original sealed containers. |
Scope note: Ceftazidime as a sterile pharma-grade API is not converted into tablet, capsule, or granule dosage forms because the beta-lactam ring and free carboxylic acid are hydrolyzed in gastric pH, resulting in negligible oral bioavailability. Downstream applications are therefore confined to sterile injectable and sterile compounding routes: single-dose dry-powder vials, continuous intravenous infusion devices, extemporaneous ophthalmic solutions, peritoneal dialysate admixtures, and pharmacy bulk partition into patient-specific parenteral units.
Sterile manufacture of ceftazidime for injection excludes terminal steam sterilisation because the beta-lactam ring hydrolyzes under saturated steam conditions at 121°C; the resulting degradation products lack antimicrobial activity. Ceftazidime pentahydrate is therefore handled as a sterile dry powder produced by aseptic crystallisation, particle size reduction, blending with sterile sodium carbonate, and filling into Type I borosilicate glass vials. The formulation addition ratio is 1 g ceftazidime activity to 118 mg sodium carbonate for the 1 g vial, 236 mg for the 2 g vial, and 708 mg for the 6 g pharmacy bulk package. The sodium carbonate functions as an alkalizing and solubilizing excipient upon reconstitution and contributes approximately 2.3 mEq sodium per gram of ceftazidime activity. The downstream production process includes vial washing, dry-heat depyrogenation, aseptic powder filling under ISO Class 5 unidirectional airflow as defined by ISO 14644-1:2015, stoppering, and crimp capping in a restricted access barrier system with dehumidified supply air. Compliance is governed by the Ceftazidime for Injection USP monograph, USP <71> sterility, USP <85> bacterial endotoxin, USP <788> particulate matter in injection, 21 CFR 211.94 container closure system requirements, and EU GMP Annex 1 for sterile manufacturing. The terminal finished product is a single-dose glass vial of ceftazidime for injection in 1 g, 2 g, or 6 g activity, intended for reconstitution before intravenous or intramuscular administration. The main operational boundary is moisture ingress during filling: exposure of the dry powder to uncontrolled humidity initiates surface hydrolysis, visible powder clumping, and a shift in reconstituted solution pH. Residual moisture acceptance criteria are product-specific and are controlled by the API manufacturer’s certificate of analysis rather than by a single universal pharmacopoeial value.
| Presentation | Ceftazidime activity | Sodium carbonate | Sodium load | Reconstitution diluent |
|---|---|---|---|---|
| Single-dose vial | 1 g | 118 mg | 2.3 mEq | 10 mL Sterile Water for Injection |
| Single-dose vial | 2 g | 236 mg | 4.6 mEq | 10 mL Sterile Water for Injection |
| Pharmacy bulk package | 6 g | 708 mg | 13.8 mEq | 26 mL Sterile Water for Injection |
For outpatient antimicrobial therapy and severe Pseudomonas aeruginosa infection where prolonged beta-lactam exposure is clinically indicated, ceftazidime is compounded into elastomeric continuous-infusion devices. The dry powder is manipulated in an ISO Class 5 compounding aseptic isolator: the 6 g vial is brought to room temperature, the rubber closure is disinfected with sterile 70% isopropyl alcohol, and 26 mL Sterile Water for Injection is introduced to yield a nominal 200 mg/mL concentrate. This concentrate is transferred to an elastomeric pump reservoir and diluted with 0.9% sodium chloride injection to a working concentration of 25 mg/mL, corresponding to 6 g ceftazidime in 240 mL. The sodium carbonate component contributes 13.8 mEq sodium per 6 g dose, a factor that must be quantified in sodium-restricted patients. The downstream production process includes sterile syringe transfer, removal of air from the elastomeric reservoir, and priming of the pump at a nominal flow rate of 10 mL/h to deliver the total volume over 24 h. Compounding compliance falls under USP <797>, and the elastomeric pump should be operated within the manufacturer’s labelled flow-rate accuracy and back-pressure limits. The terminal finished product is a wearable elastomeric infusor containing 240 mL ceftazidime 25 mg/mL in 0.9% sodium chloride. The critical process conflict is pH-dependent hydrolytic instability: ceftazidime in aqueous solution degrades more rapidly as pH rises, and above pH 8 the beta-lactam ring hydrolysis rate can reduce active content before the end of the infusion. The final solution after dilution should remain within the reconstituted pH range of 5.0 to 7.5. Incompatibility with aminoglycosides is operationally significant; ceftazidime should not be admixed with gentamicin, tobramycin, or amikacin in the same pump chamber or connected line without an intervening flush because mutual inactivation and particulate formation have been documented. Published data for ceftazidime 25 mg/mL in 0.9% sodium chloride in elastomeric devices indicate a 24 h room-temperature stability window at 25°C; body-surface temperatures above 25°C, longer dwell times, or alternative diluents require site-specific stability verification under USP <797> because published data for those configurations is limited.
When ceftazidime dry powder is used for topical ophthalmic treatment of bacterial keratitis, the sterile injectable starting material is compounded into a preservative-free fortified solution because no licensed commercial ophthalmic ceftazidime is available. The formulation addition ratio is a final ceftazidime concentration of 50 mg/mL, commonly prepared by reconstituting a 1 g vial with 10 mL Sterile Water for Injection to obtain an intermediate concentration of 100 mg/mL, then diluting to a final volume of 20 mL with preservative-free ophthalmic irrigating solution or balanced salt solution. The downstream production process is performed in an ISO Class 5 laminar-airflow hood under USP <797> low-risk compounded sterile preparation conditions; the reconstituted solution is drawn into a sterile syringe, transferred to a sterile amber ophthalmic dropper bottle, and used without terminal sterilisation. Because the preparation is intended for the eye, particulate matter is controlled according to USP <789>; sterility of the starting vial lot is verified by supplier certificate and aseptic technique rather than post-compounding sterility testing of every ophthalmic batch. The terminal finished product is a preservative-free fortified ophthalmic solution, 50 mg/mL, packaged in an amber dropper bottle and labelled with a patient-specific beyond-use date. Published data for the physicochemical stability of ceftazidime 50 mg/mL in ophthalmic vehicles is limited; several public hospital compounding protocols assign refrigerated storage between 2°C and 8°C for up to 7 days, but stability beyond this should be confirmed by validated high-performance liquid chromatography because the solution is preservative-free and sterility cannot be assumed after the first withdrawal.
Intraperitoneal administration of ceftazidime for peritoneal dialysis-associated peritonitis requires the dry sterile API to be dissolved and admixed into dialysate bags under aseptic conditions immediately before use. The formulation addition ratio depends on the dosing strategy: continuous intraperitoneal dosing uses a ceftazidime concentration of 125 mg/L to 250 mg/L in each dialysate bag, while intermittent dosing uses 1 g ceftazidime added to one 2 L bag once daily during a long dwell of at least 6 h. The downstream production process starts with reconstitution of a 1 g vial in 10 mL Sterile Water for Injection; the required volume is then injected through the dialysate bag additive port in an ISO Class 5 hood, and the bag is mixed by gentle inversion rather than shaking to avoid foam formation and possible precipitation. The compliance framework is the International Society for Peritoneal Dialysis peritonitis treatment guideline, USP <797> for sterile compounding, and the hospital’s dialysis fluid sterility policy; the receiving container is a closed, single-use, sterile dialysate bag of the type used for continuous ambulatory peritoneal dialysis or automated peritoneal dialysis. The terminal finished product is a ready-to-use intraperitoneal dialysate bag, such as a 2 L glucose-based dialysate bag containing 1 g ceftazidime, intended for immediate connection to the patient’s peritoneal catheter. Published data for ceftazidime stability in icodextrin-based dialysate is limited; in the absence of a validated stability study for that specific carrier, the admixture should be prepared in glucose-based dialysate and administered without delay. The main operational boundary is that the admixture must not be stored beyond the shortest of the drug-specific stability window and the dialysate bag label storage limit; because ceftazidime in solution is heat-labile, bags that have warmed to body temperature during patient transport are assigned a shorter beyond-use date than refrigerated bags.
When the 6 g ceftazidime pharmacy bulk package is used in a hospital sterile compounding unit, the downstream process is not reconstitution for a single patient but sequential partition of the reconstituted drug into multiple patient-specific intravenous units. The formulation addition ratio remains 1 g ceftazidime activity per 118 mg sodium carbonate, so the 6 g package contains 708 mg sodium carbonate. The production process requires the pharmacy bulk package to be accessed only in an ISO Class 5 hood under USP <797> Category 2 compounding conditions; the rubber closure is disinfected with sterile 70% isopropyl alcohol, and each dose is withdrawn with a separate sterile syringe to reduce cross-contamination risk. The terminal finished product is a series of individually labelled intravenous admixture bags prepared from the same bulk source, typically containing 1 g or 2 g ceftazidime per 50 mL to 100 mL of compatible diluent. The pharmacy bulk package is not intended for direct patient administration and must be discarded if the closure integrity is compromised, if the vial is removed from the controlled aseptic area, or if the maximum in-use time specified in the facility’s USP <797> Category 2 policy is exceeded. Published data for extended hold times of reconstituted ceftazidime 200 mg/mL in partially used pharmacy bulk packages is limited; therefore the most conservative facility-specific beyond-use allocation is applied when the same vial is used to prepare multiple scheduled doses.
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Ceftazidime (sterile) pharma grade API is a semisynthetic third-generation cephalosporin antibiotic supplied as a sterile crystalline pentahydrate powder. The material is controlled for aseptic conversion into injectable dry-powder dosage forms and for controlled granule, tablet, or capsule manufacture where the intended route is local, non-systemic, or supported by permeability-enhancing formulation data. The anhydrous molecular formula is C22H22N6O7S2, and the pentahydrate has a theoretical water content of 14.15% m/m. The product grade is defined by release data for sterility, bacterial endotoxin, particulate matter, assay, water content, residual solvents, elemental impurities, and polymorphic identity rather than by a single commercial model code.
The term “sterile pharma grade” distinguishes this material from non-sterile ceftazidime API. It is not intended for terminal sterilization after formulation, and it is released with a Certificate of Analysis including sterility per USP <71> and bacterial endotoxin per USP <85>. In parenteral manufacture, ceftazidime is commonly blended with sterile sodium carbonate at 118 mg per 1 g ceftazidime, because the carbonate adjusts reconstitution pH. The API is supplied as the pentahydrate acid; the injectable solution is formed in situ rather than as a preformed sodium salt. The oral and injectable designations therefore refer to manufacturing capability, not clinical equivalence: injectable processing is well established, while systemic oral bioavailability is not supported by conventional tablet or capsule data.
Ceftazidime cannot be autoclaved or gamma-irradiated; beta-lactam degradation and radiolytic related substances increase under terminal sterilization, so the sterile API is produced by aseptic crystallization, sterile filtration through 0.22 µm sterilizing-grade membranes, aseptic drying, and aseptic packaging. Filling operations for ceftazidime-sodium carbonate blends run in ISO 14644-1 Class 5 unidirectional-airflow zones under Grade A particle and microbiological monitoring. The dry powder fill lines are typically rotary auger or vacuum drum units with grounded contact surfaces; ceftazidime powder is cohesive and electrostatically active, and humidity is held at ≤ 35% RH to prevent caking and hydrate shifts. Fill-weight control follows USP <905> or Ph. Eur. 2.9.5. The reconstituted injectable product is checked for particulate matter per USP <788>; subvisible particle counts must meet the limits for injections. The final container-closure system uses washed Type I borosilicate glass vials and elastomeric closures meeting USP <381>. In-process bioburden data and aseptic process simulation records support the sterility claim.
Drying after aseptic crystallization is normally conducted in a vacuum dryer at a temperature not exceeding 35°C to protect the pentahydrate lattice. Terminal filter integrity is verified after the campaign by bubble point or water intrusion testing. Batch records include differential pressures, settle plates, contact plates, and particulate monitoring results. The process boundary is narrow because the API cannot be re-sterilized once the sterile container is opened; any post-sterilization blending must occur under Grade A conditions with validated transfer systems.
| Parameter | Method/Standard | Representative Release Limit |
|---|---|---|
| Appearance | Visual, Ph. Eur. 4.1.1 | White to faintly yellow crystalline powder |
| Identification | IR absorption and HPLC retention time | Matches reference standard |
| Assay | HPLC, anhydrous basis | 95.0–102.0% |
| Water | Karl Fischer, USP <921> | Theoretical 14.15%; dossier-specified pentahydrate range |
| Sterility | USP <71>, Ph. Eur. 2.6.1 | No growth |
| Bacterial endotoxins | USP <85>, Ph. Eur. 2.6.14 | ≤ 0.10 EU/mg |
| Particulate matter | USP <788> | Meets limits for parenteral dosage |
| Residual solvents | ICH Q3C, Ph. Eur. 5.4 | Class-specific limits; process-dependent |
| Elemental impurities | ICH Q3D, USP <232>/<233> | PDE-based limits |
| Polymorphic identity | XRPD | Conforms to pentahydrate reference |
The assay window of 95.0–102.0% on the anhydrous basis is established by HPLC against a reference standard; it is not a surrogate for dry weight. Water content is controlled by Karl Fischer titration per USP <921> because ceftazidime is supplied as the pentahydrate. The theoretical water content is 14.15% m/m; loss of lattice water changes reconstitution time and solid-state stability. The bacterial endotoxin limit of 0.10 EU/mg is tighter than a simple dose-based calculation for a 2 g dose over 1 h in a 70 kg adult, which yields 0.175 EU/mg per USP <85>. A tightened internal limit provides margin for infusion rates above 1 g/h or for patient weights below 70 kg.
Residual solvents are reported against ICH Q3C. Class 1 solvents, where applicable, are controlled at the general ICH limits of 2 ppm for benzene and 4 ppm for carbon tetrachloride; Class 2 solvents are controlled individually per ICH Q3C Table 2. Class 3 solvents are limited to 50 mg/day. Elemental impurities are controlled using the PDE approach of ICH Q3D and are measured by USP <232> and <233>. The pharmacopoeial identity is “Ceftazidime for Injection” when the API is incorporated into a parenteral dry powder with sodium carbonate.
Conventional immediate-release oral ceftazidime is not a routine clinical configuration; ceftazidime is acid-labile in the gastric environment and poorly absorbed across intestinal epithelia. Published systemic bioavailability data for ceftazidime tablets, capsules, or granules are limited. The API may be used in oral solid dosage manufacture only for local, non-systemic, or experimental permeability-enhanced formulations supported by pharmacokinetic data. Aqueous wet granulation is not recommended because the beta-lactam ring and pentahydrate lattice are hydrolysis-sensitive; dry granulation by roller compaction is preferred where solid dosage development is required. If tablet compression is undertaken, excipients with basic character, primary amines, or transition-metal residues should be avoided. Enteric coating alone does not confer systemic oral bioavailability; it delays acid exposure but does not overcome poor permeability.
Roller compaction and slugging are preferred over high-shear aqueous granulation. The hydraulic pressure and roll gap are controlled to minimize fines; the milled granules typically show improved flow but may require dry binder. The C-3 pyridinium substituent gives the molecule a strong dipole, and in low-humidity environments the powder can adhere to stainless steel surfaces. Equipment grounding and ionizing bars reduce static. If a capsule product is developed, low-moisture fillers such as pregelatinized starch or microcrystalline cellulose may be used, but compatibility with the oxime side chain should be screened under ICH Q1A accelerated conditions of 40°C/75% RH. Stability-indicating HPLC methods should quantify ceftazidime and specified related substances; the lactam ring can isomerize or open, and the oxime geometry can shift under UV exposure. Photostability testing per ICH Q1B is required because cephalosporin powders show light sensitivity.
Ceftazidime carries a 2-aminothiazol-4-yl oxime side chain and a C-3 pyridinium substituent. The quaternary pyridinium increases aqueous solubility but reduces activity against Gram-positive cocci relative to early cephalosporins. Ceftazidime is differentiated from ceftriaxone by low protein binding of 10–17% versus 85–95%, and by predominant renal elimination as unchanged drug. Ceftriaxone relies more on biliary excretion and has specific neonatal contraindications related to calcium precipitation; ceftazidime does not share that restriction. Ceftazidime is differentiated from cefotaxime by the absence of a therapeutically active desacetyl metabolite; cefotaxime is partially metabolized to desacetylcefotaxime. Compared with cefepime, a fourth-generation cephalosporin, ceftazidime is more susceptible to hydrolysis by derepressed AmpC beta-lactamases. Ceftazidime is not ceftazidime-avibactam; the latter is a co-formulated product with the non-beta-lactam beta-lactamase inhibitor avibactam.
| Attribute | Ceftazidime | Ceftriaxone | Cefepime |
|---|---|---|---|
| Class | Third-generation | Third-generation | Fourth-generation |
| Protein binding | 10–17% | 85–95% | 16–20% |
| Primary elimination | Renal unchanged | Biliary and renal | Renal unchanged |
| Antipseudomonal activity | Yes | No or weak | Yes |
| C-3 substituent | Pyridinium | Triazinyl-thiomethyl | N-Methylpyrrolidinium |
Compared with cefoperazone, ceftazidime lacks the N-methylthiotetrazole side chain and therefore is not associated with disulfiram-like reactions or hypoprothrombinemia. Antipseudomonal activity is assessed by MIC breakpoints in CLSI M100 and EUCAST susceptibility standards. The manufacturing differences are also material: ceftazidime injection uses sodium carbonate to adjust pH, while ceftriaxone injection is commonly supplied as a disodium salt derivative that does not require that carbonate blend. The ceftazidime pyridinium form demands control of pH and avoidance of anionic excipients that can form insoluble complexes.
Ceftazidime pentahydrate should be stored at 15–25°C in well-closed, light-resistant containers. The dispensing suite for injectable filling should be held at ≤ 35% RH and 18–22°C; excursions above 60% RH promote caking and static discharge. Contact surfaces should be 316L stainless steel or PTFE-lined; iron, copper, and zinc ions can catalyze beta-lactam degradation. The powder is not suitable for autoclave or radiation sterilization after formulation. Pre-drying the pentahydrate is not recommended, because loss of lattice water converts the solid form and changes reconstitution behavior. Ceftazidime solutions are incompatible with aminoglycosides, vancomycin, and strongly alkaline fluids; separate infusion lines are required. The vial may develop positive pressure during reconstitution when sodium carbonate is present, and manufacturing instructions should require venting. Use of the API in oral solid dosage forms is operationally feasible only when dry processing is used and systemic bioavailability is not the acceptance criterion.
For injectable manufacture, the product is aseptically transferred into a dry powder blend with sterile sodium carbonate. The blend is filled under nitrogen-purged conditions where static charge is high. In-line checkweighers and vacuum drum dwell times are adjusted for the poor flow and low bulk density of the ceftazidime-sodium carbonate mixture. The operational boundary is aseptic: once the sterile API is exposed to the filling environment, the line must remain within Grade A conditions, and personnel interventions must be documented and justified. Non-sterile ceftazidime API with an identical HPLC assay is not interchangeable with the sterile grade because sterility, endotoxin, particulate burden, and container-closure integrity are not retroactively achievable.