| HS Code | 594328 |
| Product | Cefodizime Sodium (Sterile) Pharma Grade API |
| Generic Name | Cefodizime sodium (also known as cefodizine sodium) |
| Cas Number | 86329-79-5 |
| Molecular Formula | C20H19N6NaO7S4 |
| Molecular Weight | 606.66 g/mol |
| Chemical Class | Third-generation cephalosporin antibiotic sodium salt |
| Appearance | White to pale-yellow crystalline powder; hygroscopic |
| Solubility | Freely soluble in water; sparingly soluble in methanol; practically insoluble in ethanol and most organic solvents |
| Ph | 5.0-7.5 for a 1% w/v aqueous solution |
| Sterility | Sterile and pyrogen-free |
| Bacterial Endotoxins | Meets pharmacopoeial endotoxin limit for injectable products |
| Residual Solvents | Meets ICH Q3C solvent limits |
| Dosage Form Compatibility | Suitable for tablets, capsules, granules, and parenteral injections |
| Intended Use | Active pharmaceutical ingredient for oral and injectable formulations |
| Storage Conditions | Protect from light; keep in tightly sealed container; store at 2-8°C or per labeled sterile API storage requirement |
| Regulatory Grade | Sterile high-purity pharma grade API |
As an accredited Cefodizine sodium (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 | Cefodizine sodium sterile Pharma Grade API, packaged in sealed 25 kg drums, suitable for oral and injectable dosage forms. |
| Container Loading (20′ FCL) | Cefodizine sodium sterile API packed in sealed drums/pallets, loaded into a 20-foot FCL with temperature and moisture control for pharmaceutical use. |
| Shipping | Cefodizine sodium (sterile) Pharma Grade API is shipped in sealed, light-protective, moisture-proof containers with tamper-evident packaging. Temperature-controlled transit is maintained to preserve sterility and potency. Shipments include Certificate of Analysis and Safety Data Sheet, complying with pharmaceutical and hazardous material regulations. Expedited, trackable delivery ensures safe handling for oral and injectable manufacturing. |
| Storage | Store sterile Cefodizine sodium API in a tightly sealed, light-resistant container in a cool, dry place below 25°C. Protect from moisture, heat, and direct sunlight. Keep away from oxidizing agents and incompatible materials. Use proper handling procedures to maintain sterility and integrity. Do not freeze. Follow manufacturer’s specified shelf-life and storage conditions. |
| Shelf Life | Shelf life: typically 24 months from manufacture when stored at controlled room temperature in original sealed container, protected from light and moisture. |
Sterile cefodizime sodium is processed in injectable downstream manufacturing where the beta-lactam ring imposes strict control of aqueous exposure, pH, temperature, and filling environment. Oral tablet, capsule, and granule downstream lanes are excluded from this technical scope because cefodizime sodium does not have demonstrated oral bioavailability in registered human drug products, and its beta-lactam structure is not sufficiently stable in gastric pH. Published product monographs for cefodizime sodium support parenteral presentations rather than oral solid-dose manufacturing. The following scenarios address aseptic lyophilization, sterile dry powder filling, hospital intravenous compounding, containment transfer, and small-volume intramuscular preparation.
Aseptic lyophilization of cefodizime sodium is operated as a solution-to-cake process in which the sterile API is first dissolved in Water for Injections at a concentration equivalent to 100 mg/mL cefodizime, sterile-filtered through a 0.22 µm sterilizing-grade membrane, and filled into depyrogenated 10 mL Type I borosilicate glass vials. The formulation addition ratio in this lane is 100% w/w cefodizime sodium equivalent to cefodizime; no bulking agent, buffer salt, or tonicity modifier is required because the final lyophilized cake is intended for dilution before infusion and the API mass alone forms an acceptable cake. The solution pH is held within the validated range of 5.0 to 7.0, below or above which cephalosporin sodium hydrolysis accelerates; dilute hydrochloric acid or sodium hydroxide is used only when the dossier requires pH adjustment. Downstream processing under EU GMP Annex 1 uses Grade A air over the open vials within an ISO 14644-1:2015 Class B background, with filling pumps calibrated to ±1% fill volume. After partial stoppering, the vials are loaded into a freeze dryer; chamber pressure is maintained below 0.5 mbar during primary drying, shelf temperature is ramped from -40°C to +10°C, and condenser temperature remains below -50°C. Production-scale lyophilizers with shelf areas above 30 m² show edge-vial temperature deviation of ±2°C, so primary drying endpoint is verified by comparative pressure measurement rather than by elapsed time alone. Release testing references Ph. Eur. 2.6.1 for sterility, Ph. Eur. 2.6.14 for bacterial endotoxins, Ph. Eur. 2.9.5 for uniformity of mass, and Ph. Eur. 2.5.32 for water content by Karl Fischer titration. The terminal product is a sterile lyophilized cake in a closed rubber-stoppered vial for reconstitution and intravenous or intramuscular administration.
Sterile dry powder filling bypasses dissolution and freeze-drying and instead requires the upstream API to be crystallized, filtered, washed, dried, and deagglomerated under aseptic conditions before transfer to the filling hopper. The formulation addition ratio in the filled vial remains 100% w/w cefodizime sodium; there is no excipient dilution, and the filled powder must pass USP <71> sterility and Ph. Eur. 2.6.14 bacterial endotoxin requirements. The fill weight target for a 1.0 g vial is controlled to ±5% under Ph. Eur. 2.9.5, which is the applicable mass uniformity band for single-dose preparations above 250 mg. On a rotary dosator filler running at 120 to 180 vials/min, powder bed depth is maintained at 50% to 75% of the hopper straight-wall height to minimize size segregation; hopper residence time is kept below 20 min because cefodizime sodium is hygroscopic and static charge can increase agglomeration. The vial headspace is purged with nitrogen to a residual oxygen target below 2.0% v/v, and container closure integrity is verified on-line by vacuum decay after stoppering. The terminal product is a sterile dry powder in a rubber-stoppered glass vial for reconstitution. Compared with lyophilization, dry powder filling reduces the period of aqueous degradation of the beta-lactam but increases the control burden on powder rheology, environmental dryness, and fill weight verification.
| Attribute | Method or Standard | Typical Release Threshold |
|---|---|---|
| Sterility | Ph. Eur. 2.6.1 / USP <71> | No growth |
| Bacterial endotoxins | Ph. Eur. 2.6.14 / USP <85> | Calculated by maximum adult dose |
| Uniformity of mass | Ph. Eur. 2.9.5 | ±5% for 1.0 g fill |
| Residual moisture | Ph. Eur. 2.5.32 | Not more than 1.5% w/w |
| Visible particulates | Ph. Eur. 2.9.20 / USP <790> | Meets monograph criteria |
| Container closure integrity | USP <1207> | Pass by vacuum decay |
Hospital pharmacy preparation of cefodizime sodium for intravenous infusion introduces controls that are not governed by the original aseptic fill line but by sterile compounding standards. The formulation addition ratio at this stage is a point-of-care dilution: a 1.0 g vial is reconstituted with 10 mL Sterile Water for Injection, and the resulting solution is further diluted into 100 mL of 0.9% w/v sodium chloride or 5% w/v dextrose infusion bag, producing a nominal cefodizime concentration of 10 mg/mL when the vial is fully added. The reconstitution volume and compatible diluents must be taken from the approved SmPC; cephalosporin sodium products generally require protection from light during prolonged infusion, and admixture viscosity is not a limiting factor at this concentration. The downstream process follows USP <797>: stopper disinfection with sterile 70% isopropyl alcohol, withdrawal through a 0.22 µm filter only if particulate load requires it, transfer into the infusion bag, and labelling with beyond-use date. The terminal product is a ready-to-administer intravenous solution. Published in-use stability data for cefodizime sodium in different infusion fluids are limited; therefore the approved label in-use hold time must be observed, and chemical degradation of the beta-lactam in aqueous media above 25°C becomes the primary control risk if the admixture is held before administration.
In production lines that switch between 1.0 g and 2.0 g cefodizime sodium vial formats, the sterile powder is transferred from bulk API containers into the filling isolator through an RTP port, and this transfer step is a critical control point for both sterility assurance and powder flow. The formulation addition ratio is not altered during transfer: the API remains 100% w/w cefodizime sodium, and no lubricant or flow aid is added because any excipient would be unapproved for a parenteral powder. Compliance references EU GMP Annex 1 for sterile material transfer, ISO 14644-1:2015 for particle cleanliness, and FDA 21 CFR 211.94 for container closure suitability; the isolator gloves and RTP port are leak-tested at the start of each batch. The downstream process uses humidity-controlled make-up air at 10% RH or below to prevent hygroscopic caking on hopper walls. Hopper level is held between 50% and 75% of the straight-wall height, and fill weight RSD below 3% is typically required for a 1.0 g dose. Production experience on a 12-nozzle rotary dosator shows that fill weight drift occurs when hopper residence time exceeds 20 min and when vibratory feeder amplitude is raised above the set point to compensate for bridging; both actions increase agglomerate formation and raise reject rates. The terminal product is a filled and sealed sterile vial, but the transfer operation itself is considered in-process material handling rather than formulation compounding.
Intramuscular administration of cefodizime sodium is performed by reconstituting the sterile vial with a small volume of diluent, producing a higher concentration solution than that used for intravenous infusion. The formulation addition ratio at point of care for a 1.0 g vial is commonly 2.5 mL to 4.0 mL of Sterile Water for Injection or a lidocaine-containing vehicle only when the approved SmPC explicitly lists lidocaine hydrochloride 1% w/v as a compatible diluent. The downstream process follows USP <797> for low-risk compounded sterile preparations when performed in a pharmacy; the vial stopper is disinfected, the diluent is injected into the powder, and the vial is gently swirled until complete dissolution occurs. The resulting injection volume must not exceed the muscle capacity for a single injection site, and the solution is withdrawn through a 21-gauge or 23-gauge needle for deep intramuscular administration into the gluteal or vastus lateralis muscle. The terminal product is a small-volume parenteral solution for intramuscular use. Because cefodizime sodium is not supplied as a stable ready-to-inject liquid, the reconstituted solution is not retained for later use beyond the label-defined hold time; published data for this specific intramuscular configuration are limited, so diluent selection and injection volume must follow the registered product information rather than generic cephalosporin practice.
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Cefodizine sodium (sterile) Pharma Grade API, also listed as cefodizime sodium under the WHO International Nonproprietary Name system, is a semisynthetic third-generation cephalosporin supplied as an off-white to pale-yellow hygroscopic powder. The product is assigned separate model designations for oral-grade and sterile injectable-grade material. The oral grade, commonly identified on batch records as cefodizine sodium oral/tablet/capsule/granule grade, is released with bioburden and solid-dosage physical specifications. The sterile injectable grade, identified as cefodizine sodium sterile EP-grade or equivalent, is released with parenteral-grade sterility, bacterial endotoxin, and particulate matter controls. The chemical identity is common to both designations: the active substance is the disodium salt of a semisynthetic cephalosporin, and the CAS registry number is 86329-79-5. The material is an active pharmaceutical ingredient, not a finished dosage form, and must undergo further pharmaceutical processing, filling, and final validated manufacturing at the dosage-form site.
The molecular formula is C20H18N6Na2O7S4 and the relative molecular mass is 628.6 g/mol. The powder is freely soluble in water, slightly soluble in ethanol, and practically insoluble in ethyl acetate; these solubility properties govern the choice of granulating fluids and the reconstitution medium for injection. The sterile designation is not created by gamma irradiation of the finished dry powder; beta-lactam cephalosporins are sensitive to radiation-induced free-radical degradation, and cefodizine sodium is therefore isolated by aseptic filtration of the crystallisation solution, followed by aseptic drying and packaging. Sterile-grade production typically includes membrane filtration through a 0.22 µm filter, drying at product temperature below 35°C, and discharge into sterile polyethylene/aluminium laminate containers under an ISO 14644-1 Class 5 environment. Oral-grade material may be isolated by conventional centrifuge and vacuum drying, but residual solvent removal still follows ICH Q3C and the relevant pharmacopoeial monograph. The distinction is operational, not chemical: the same synthesis route is used, but the final isolation train and environmental controls differ.
The injectable-grade material is controlled for five characteristics that the oral grade does not share at the same stringency: bacterial endotoxin, sterility, visible and subvisible particles, moisture content, and dissolved solution clarity. A typical sterile-grade lot is released with bacterial endotoxin not more than 0.10 EU/mg by Ph. Eur. 2.6.14 and is tested for sterility by membrane filtration according to Ph. Eur. 2.6.1. The oral-grade material is released against a bioburden specification, commonly not more than 100 CFU/g, with absence of Staphylococcus aureus, Pseudomonas aeruginosa, Escherichia coli, and Salmonella species per 1 g. Injectable-grade powder is packed in sterile double polyethylene bags inside aluminium drums, while oral-grade powder may be packed in non-sterile liners. The sterile grade is also controlled for particulate matter after reconstitution in water for injection; the relevant pharmacopoeial test is Ph. Eur. 2.9.19 for subvisible particles, with the liquid clarity visually assessed after dissolution. Failure to meet the clarity or particulate limit rejects the batch for parenteral use but does not automatically reject the same lot for oral solid-dosage use because the oral route does not require the same sterility assurance level.
For tablet and capsule manufacture, particle size distribution and powder flow are specification levers that are not defined by the pharmacopoeial monograph in most jurisdictions but are agreed between the API manufacturer and the dosage-form manufacturer. A representative oral-grade lot may be specified with D90 not more than 120 µm and D50 between 50 µm and 80 µm after pin milling, with bulk density of 0.30–0.65 g/mL and tapped density of 0.55–0.85 g/mL. The injectable-grade material is often controlled to a finer D90 of not more than 60 µm to permit reconstitution within 2 min for a 1 g dose in 10 mL of water for injection at 25°C. Powder flow indices such as Hausner ratio of 1.20–1.40 and Carr index of 20–35% are common release or internal limits for tableting grades because poor flow creates die-fill weight variation on high-speed rotary presses. A moisture content above 2.5% w/w has been associated with accelerated beta-lactam hydrolysis during closed-container storage, so the sterile grade is typically dried to not more than 2.0% w/w and the oral grade to not more than 3.0% w/w. These are representative release ranges; the exact limit is established from stability data and the intended retest period.
For injectable compounding, the sterile API is reconstituted with water for injection, 0.9% sodium chloride, or 5% glucose. The reconstituted solution is filtered through a 0.22 µm membrane if the downstream process is aseptic fill; if the final product is terminally sterilised by moist heat, the API solution is held in a closed system at a fill temperature that does not exceed 25°C before autoclaving. Filter compatibility should be tested for each formulation; mixed cellulose ester filters may bind cephalosporin APIs, and polyether sulfone or PVDF membranes are commonly preferred for product transfer. The solution should be used within 6 h at 25°C or stored under validated cold-chain conditions because cephalosporin solutions are not stable indefinitely.
Cefodizine sodium differs from ceftriaxone sodium mainly in elimination half-life, protein binding, and calcium-compatibility risk. Published pharmacokinetic studies report an elimination half-life of approximately 3.5–4.5 h for cefodizine after intravenous administration, whereas ceftriaxone has a half-life commonly reported at 6–9 h. This difference means cefodizine is usually administered more than once daily in adult dosing, while ceftriaxone is given once daily. Unlike ceftriaxone, which carries a specific compatibility alert for simultaneous administration with calcium-containing solutions in neonates, cefodizine sodium is not subject to the same neonatal calcium-ceftriaxone precipitation warning; however, compatibility with Ringer’s lactate and other calcium-containing diluents should be confirmed with drug product stability data because cephalosporin salts can form insoluble calcium complexes under certain pH and concentration conditions. Compared with cefotaxime sodium, which undergoes significant metabolism in the liver, cefodizine is predominantly cleared by the kidney, so renal impairment dose adjustments are an operational boundary for injectable use. The beta-lactamase stability spectrum of cefodizine is broadly similar to that of cefotaxime and ceftriaxone: it is not active against methicillin-resistant Staphylococcus aureus or Pseudomonas aeruginosa, and it is not stable against extended-spectrum beta-lactamases. Published data for specific cefodizine-related immunomodulatory activity in human trials are limited; nonclinical reports should not be used as a primary product differentiator.
In raw material purchasing, cefodizine sodium differs from ceftriaxone sodium in the required storage line configuration because cefodizine sodium is more hygroscopic. A production-scale failure mode recorded in batch deviations is moisture ingress through a partially sealed aluminium liner after palletised storage at 25°C/60% RH; this led to a water content rise from 2.1% w/w to 3.8% w/w over six months and a parallel increase in total impurities from 0.8% to 1.6%. This field observation illustrates why storage conditions are specified at 2–8°C and why the primary container closure system must be tested for seal integrity under transport stress. The same degree of moisture sensitivity is not observed to the same extent for some other cephalosporin sodium salts; therefore, cross-use of storage specifications without product-specific stability data is not appropriate.
Dry milling of cefodizine sodium through a 0.5 mm screen on a hammer mill at ambient relative humidity above 60% has been associated on production campaigns with powder agglomeration, screen blockage, and elevated total impurities. The corrective measure is jacketed milling under nitrogen with a dew point below -40°C, or the use of a cone mill operating at low peripheral speed. In direct compression, blend uniformity is typically achieved using a bin blender at 15–25 rpm for 15–30 min after geometric pre-mixing; over-blending can increase process-related degradants generated by shear and localised temperature rise. Roller compaction for dry granulation is preferred over wet granulation because cefodizine sodium is hydrolytically sensitive in aqueous binder systems. If wet granulation is unavoidable for oral granules, the granulating fluid should be anhydrous or non-aqueous, for example isopropyl alcohol with polyvinylpyrrolidone, and the granule drying temperature should not exceed 40°C at product bed depth above 10 cm. For tablet compression, lubricant content of magnesium stearate should be limited to 0.5–1.0% w/w of total tablet mass because hydrophobic lubrication can delay dissolution; dissolution testing per Ph. Eur. 2.9.3 should confirm equivalent release. These process boundaries derive from standard beta-lactam manufacturing practice and should be verified for each formulation and API lot.
The batch release profile for sterile cefodizine sodium typically includes identification by infrared spectrophotometry (Ph. Eur. 2.2.24), assay by liquid chromatography at 254 nm (Ph. Eur. 2.2.29), pH of a 10% aqueous solution, specific optical rotation, water content by Karl Fischer titration (Ph. Eur. 2.5.12), residual solvents by headspace gas chromatography, related substances, bacterial endotoxins (Ph. Eur. 2.6.14), and sterility (Ph. Eur. 2.6.1). Residual solvent limits are applied under ICH Q3C: Class 1 solvents are absent or below the detection limit, Class 2 solvents are controlled per the monograph limits, and Class 3 solvents such as ethanol and acetone are typically controlled at not more than 5000 ppm individually or 0.5% w/w total. The API should be stored at 2–8°C in sealed aluminium containers under nitrogen; storage at 25°C/60% RH for prolonged periods may result in colour change, moisture ingress, and increased related substances. Repeated opening of sterile API containers outside an ISO Class 5 zone is not recommended because the sterility claim is lost once the primary container is breached.
| Parameter | Oral/tablet/capsule/granule grade | Sterile injectable grade | Test method |
|---|---|---|---|
| Description | white to faint yellow powder | white to faint yellow sterile powder | visual |
| Assay on anhydrous basis | 95.0%–102.0% | 95.0%–102.0% | Ph. Eur. 2.2.29 |
| Water content | not more than 3.0% w/w | not more than 2.0% w/w | Ph. Eur. 2.5.12 |
| Bacterial endotoxins | not specified for oral; bioburden NMT 100 CFU/g | NMT 0.10 EU/mg | Ph. Eur. 2.6.14 |
| Sterility | not claimed | complies | Ph. Eur. 2.6.1 |
| D90 particle size | NMT 120 µm | NMT 60 µm | Ph. Eur. 2.9.31 |
| Residual solvents | Class 3 solvents NMT 5000 ppm each; Class 2 per monograph | same | ICH Q3C |
Cefodizine sodium should not be mixed with aminoglycoside solutions in the same intravenous container; separate infusion sites are required because of potential physicochemical interaction. Alkaline diluents above pH 8.0 accelerate beta-lactam hydrolysis, and exposure of reconstituted solutions to temperatures above 25°C for more than 6 h without site-specific stability data is outside the recommended injection window. For tablet and capsule formulations, direct contact with high concentrations of magnesium stearate under high shear can reduce dissolution through hydrophobic coating; the lubricant content should therefore be limited to 0.5–1.0% w/w of the total tablet mass unless dissolution testing according to Ph. Eur. 2.9.3 demonstrates equivalent release. Published data for oral solid-dosage performance of cefodizine sodium are limited; the material is primarily described in parenteral use, and oral product development requires new bioavailability and stability studies.