| HS Code | 268640 |
| Product Name | Latamoxef Sodium (Sterile) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Api Name | Latamoxef Sodium |
| Grade | Pharma Grade (Sterile) |
| Sterility | Sterile |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Route Of Administration | Oral and Injectable |
| Chemical Formula | C20H18N6Na2O9S |
| Molecular Weight | 564.44 g/mol |
| Cas Number | 64953-12-4 |
| Appearance | White to pale yellowish crystalline powder |
| Solubility | Soluble in water; slightly soluble in methanol; practically insoluble in most organic solvents |
| Storage Condition | Store in airtight containers in a cool, dry place; protect from light and moisture |
| Therapeutic Category | Antibiotic (Oxacephem) |
| Description | A semi-synthetic oxacephem antibiotic with broad-spectrum activity against Gram-positive and Gram-negative bacteria, intended for pharmaceutical formulation in oral and injectable dosage forms. |
As an accredited Latamoxef 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 | Sterile Latamoxef Sodium API packed in sealed double polyethylene bags inside aluminum foil bag and fiber drum, 10 kg net quantity. |
| Container Loading (20′ FCL) | One 20′ FCL containing Latamoxef Sodium sterile Pharma Grade API, packed securely for oral and injectable pharmaceutical use. |
| Shipping | Shipment of Latamoxef Sodium (sterile) is conducted in temperature-controlled, sealed containers to maintain purity and stability. It is packaged in airtight, moisture-resistant drums or bags, protected from light. Documentation includes COA, MSDS, and handling guidelines. Shipping complies with pharmaceutical and safety regulations for oral and injectable API transport. |
| Storage | Store Latamoxef Sodium (sterile) Pharma Grade API in tightly sealed, moisture-proof containers, protected from light, at controlled room temperature (15–30°C) or as per label. Keep in a cool, dry, well-ventilated area away from incompatible substances. For sterile grades, maintain container integrity and handle aseptically to preserve sterility. |
| Shelf Life | Shelf life: 36 months when stored as directed in original container, protected from moisture, heat, and light. |
Latamoxef sodium (sterile) is not established as a commercial oral tablet, capsule, or granule dosage form because the oxacephem nucleus undergoes acid-catalyzed hydrolysis in gastric fluid and published oral bioavailability data for this specific configuration is limited. The milled sterile granule fraction described in the API specification is used as dry powder feed for parenteral filling lines; the application scenarios below are therefore limited to sterile injectable manufacturing and hospital admixture routes.
Reconstitution of latamoxef sodium is governed less by the intrinsic aqueous solubility of the oxacephem sodium salt than by powder bed architecture, vial headspace composition, solvent temperature, and stopper surface treatment. A 1.0 g fill mass is reconstituted with 10 mL Water for Injection to produce 100 mg/mL; a 2.0 g fill mass is reconstituted with 20 mL Water for Injection to deliver the same 100 mg/mL concentration. The terminal finished product type after reconstitution is a solution for intravenous infusion or, where national labeling permits, intramuscular injection after appropriate dilution. The downstream production step in the hospital or licensed compounding unit occurs inside an ISO 14644-1:2015 Class 5 environment or Grade A unidirectional airflow cabinet, using a vented reconstitution device to equalize vial headspace pressure and reduce aerosol loss from the stopper puncture site. Water for Injection is typically conditioned to 20–25 °C before addition; colder solvent can reduce the dissolution rate and increase the apparent reconstitution time.
A collapsed powder plug formed during transport can delay wetting because solvent tends to channel around a dense mass rather than permeate the interstitial void space. Vials filled under a nitrogen headspace exhibit slower pressure equilibration during solvent addition unless a hydrophobic vent is used; vacuum-assisted reconstitution devices can decrease foaming but may increase stopper coring if the needle path is off-axis or the closure is over-siliconized. Release-side particulate control is anchored to Ph. Eur. 2.9.19 and USP <788> by light obscuration, while visible particle inspection follows Ph. Eur. 2.9.20. The formulation addition ratio at the pharmaceutical manufacturer is 100% w/w active latamoxef sodium with no buffering or bulking excipient; the reconstitution ratio is the hospital-side addition step that determines final dosing concentration.
Aseptic dry powder filling of latamoxef sodium into hydrolytic resistance Type I tubular glass vials is performed without bulking excipients because the sodium salt provides the entire declared active content. The fill mass is set to 1.000 g or 2.000 g net weight with an in-process gravimetric tolerance of ±5 mg on checkweigher-linked filling stations. Terminal finished product type is a dry powder for solution for injection or infusion in single-dose glass vials. The downstream process begins with vial washing in ≥70 °C Water for Injection, followed by dry heat depyrogenation at 250 °C for 30 min in a tunnel with Grade A cooling; the sterile API is sifted through a 1.0 mm stainless steel screen and filled under ≤25% relative humidity to prevent moisture-induced caking. A rotary vacuum drum filler or auger doser with 316L stainless steel product-contact parts and electropolished surface finish is used for fill weight control, and vials are sealed with siliconized bromobutyl closure under Grade A before aluminum cap crimping. Failure modes on rotary vacuum drum fillers include powder bridging in the hopper, fill weight drift caused by vacuum leakage at the dosing shoe, and electrostatic adhesion to plastic contact parts; these are managed by gravimetric checkweighing feedback and dehumidified air.
The relevant industry compliance matrix includes EU GMP Annex 1 cleanroom classification, ISO 14644-1:2015 Grade A/ISO 5 during exposed filling, Ph. Eur. 2.6.1 sterility testing, Ph. Eur. 2.6.14 bacterial endotoxin testing, USP <71>, USP <85>, and USP <788> particulate matter. The following control-point matrix summarizes the critical release and process standards for the dry powder injectable route.
| Control point | Standard or method | Equipment condition |
|---|---|---|
| Sterility | Ph. Eur. 2.6.1 / USP <71> | Membrane filtration in Grade A environment |
| Bacterial endotoxins | Ph. Eur. 2.6.14 / USP <85> | Kinetic chromogenic LAL |
| Particulate matter | Ph. Eur. 2.9.19 / USP <788> | Light obscuration particle counter |
| Water content | USP <921> Karl Fischer | Coulometric oven method |
| Glass packaging | USP <660> / Ph. Eur. 3.2.1 | Type I borosilicate tubular glass, washed and depyrogenated |
Operational boundary: the API itself is not subjected to dry heat terminal sterilization because the oxacephem nucleus is heat-labile; moisture control is therefore placed on glass, stoppers, and environmental air rather than on drying the active. If ambient RH exceeds 40%, stopper bowls and vial cooling zones are pre-conditioned with dehumidified air. Published data for the exact water activity threshold at which powder adhesion to stainless steel contact parts occurs during continuous filling is limited.
After reconstitution, the 100 mg/mL solution is transferred into 0.9% w/v sodium chloride polyolefin or PVC-free flexible bags. A 1.0 g vial added to 100 mL diluent yields 10 mg/mL; a 2.0 g vial in 100 mL yields 20 mg/mL. The terminal finished product type is a ready-to-administer intravenous infusion solution. The downstream production process at hospital pharmacies includes aseptic transfer under ISO 14644-1:2015 Class 5 conditions, serial bag port disinfection, and in-process visual inspection for particulate matter after the final admixture is prepared.
The industry compliance standard for extemporaneous admixture is USP <797> in U.S. compounding settings, while licensed preparation follows EU GMP Annex 1. Storage beyond-use dating is assigned according to the site’s USP <797> category and the national product label; published data for prolonged storage of latamoxef sodium at 20 mg/mL in 0.9% sodium chloride beyond labeled conditions is limited. Operational incompatibility: latamoxef sodium should not be admixed in the same container with aminoglycoside antibiotics because beta-lactam antibiotics can inactivate aminoglycosides through ring-opening adduct formation; separate infusion lines are used, or the lines are flushed between agents.
Container closure integrity and moisture exclusion after stopper insertion are controlled through torque-calibrated aluminum cap crimping, vision inspection for cap ovality and elastomer positioning, and seal integrity qualification using vacuum decay or dye penetration. The specified fill masses remain 1.0 g and 2.0 g; the terminal finished product type is a single-dose dry powder vial. The downstream production step after capping includes automatic weight check, oxygen headspace sampling where required, tray loading, cartoning, and storage protected from light. The closure system is qualified under USP <381> for elastomeric closure integrity and under USP <1207> for container closure integrity; glass vials are specified against USP <660> and Ph. Eur. 3.2.1. Failure of the capping station to maintain crimp deflection within validated limits can permit moisture ingress and reduce sterility assurance; a leak rate determined by vacuum decay is therefore used as the primary non-destructive release test rather than visual inspection alone. Batch-to-batch variance in closure dimensions, particularly cap skirt angle and elastomer siliconization level, has required capping station path adjustments; stopper supplier dimensional reports are therefore transferred into line setup.
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Latamoxef Sodium (sterile) Pharma Grade API is a dual-route active pharmaceutical ingredient specified for tablet, capsule, granule, and injectable formulation. The product is supplied as a sterile pharmaceutical-grade sodium salt and is identified for regulatory correspondence by CAS 64953-12-4 and molecular weight 564.44 g/mol; the molecular formula C20H18N6Na2O9S describes the disodium salt of the oxacephem nucleus. Unlike conventional cephalosporin sodium salts, the oxacephem ring replaces sulfur with oxygen at position 1 and carries a 7α-methoxy substituent. This structural arrangement modifies the hydrolytic and β-lactamase degradation pathways that govern both formulation stability and clinical spectrum.
The product model designation covers two release modes: sterile API for injectable presentations and pharma-grade API for oral dosage forms manufactured under non-sterile conditions. The sterile grade is tested against pharmacopoeial sterility and endotoxin requirements; the oral grade follows the same chemical purity and related substances profile but may be released without a sterility claim when the finished product is a tablet, capsule, or granule regulated by non-sterile microbiological criteria. Because the sodium salt is freely water-soluble and hygroscopic, packaging, storage, and dispensing controls are part of the product specification rather than optional handling notes.
| Attribute | Test method or equipment | Route rationale |
|---|---|---|
| Sterility | Membrane filtration; Ph. Eur. 2.6.1, USP <71> | Injectable formulations only; oral solids use USP <1111> microbiological limits |
| Bacterial endotoxins | Limulus amebocyte lysate; Ph. Eur. 2.6.14, USP <85> | Parenteral dose-proportional limit |
| Water content | Karl Fischer titration; Ph. Eur. 2.5.12, USP <921> | Hydrolytic degradation control |
| Related substances | HPLC; Ph. Eur. 2.2.29, USP <621> | Degradation product and impurity control |
| Particle size distribution | Laser diffraction; ISO 13320-1:2020 | Blend uniformity, dissolution, syringeability, filling accuracy |
| Residual solvents | Headspace gas chromatography; USP <467>, ICH Q3C | Safety threshold for volatile process solvents |
| Crystalline form | XRPD; USP <941> | Polymorphic consistency and stability equivalence |
The replacement of sulfur by oxygen at position 1 shifts the ring system from a cephalosporin to an oxacephem. The 7α-methoxy group introduces steric and electronic effects that reduce recognition by certain serine β-lactamases and extend the compound’s activity against selected Gram-negative anaerobes, particularly Bacteroides fragilis. The 3'-N-methyltetrazole thiol side chain contributes to antimicrobial activity but is also linked to hypoprothrombinemia and disulfiram-like reactions after alcohol exposure. This intrinsic side-effect boundary is not a formulation defect; it differentiates Latamoxef Sodium from ceftriaxone sodium and cefotaxime sodium APIs and requires prescribing information to include vitamin K monitoring when clinically indicated. From a chemical control perspective, the oxacephem nucleus and NMTT side chain require tighter related substances monitoring than first-generation cephalosporin sodium salts because trace hydrolytic products can form in aqueous solution and generate color or particulate matter. HPLC methods using C18 stationary phases, high aqueous mobile phases, and ultraviolet detection are commonly applied; method validation follows ICH Q2(R1) and USP <621>. Published data for the specific degradation products of this API are available in pharmacopoeial monographs and registration dossiers; impurity thresholds are set according to ICH Q3A and Q3B exposure limits.
Residual solvent profiles in multi-step synthesis often include acetone, ethyl acetate, or isopropanol; these are controlled as Class 3 solvents under ICH Q3C. If higher-risk solvents are used in the final crystallization or drying stages, their limits are set to a concentration corresponding to no more than the permitted daily exposure. Residual elemental impurities are tested by compendial procedures such as USP <232>/<233>; the sodium salt is not considered interchangeable with cephalosporin sodium salts that carry a different counterion profile or different residual solvent specifications without comparative release data.
Injectable presentations of Latamoxef Sodium (sterile) API are filled as dry powder or lyophilized cake in vials. Terminal steam sterilization is generally unsuitable because the β-lactam ring undergoes hydrolysis at elevated temperature. Aseptic processing therefore starts with sterile API and proceeds through sterile filtration of the dissolved drug, sterile transfer, and filling under Grade A unidirectional airflow in an isolator or restricted access barrier system. EU GMP Annex 1 cleanroom limits and ISO 14644-1 classification apply; media fills and container closure integrity testing are part of the injection-line qualification. The filling solution is typically maintained at 2–8 °C to suppress hydrolytic degradation during batch hold time. Before aseptic filling, the API is de-lumped through a sterile sieve with mesh openings in the 0.5 mm to 1.0 mm range; this step reduces agglomerates that would otherwise obstruct dosing nozzles or dissolve slowly during reconstitution. Powder flow for vial filling is characterized by bulk density and conditioned density rather than by single-particle size alone. Vacuum dosator fillers and auger fillers require specification of both loose and tapped density because variations in these values alter fill weight and dose uniformity across the batch.
Lyophilized presentations require a formulation matrix that protects the API during freezing and primary drying. Bulking agents such as mannitol or glycine may be used, but their compatibility with the sodium salt should be confirmed by differential scanning calorimetry and freeze-drying microscopy. Collapse temperature and glass transition temperature of the maximally freeze-concentrated solution determine the primary drying shelf temperature; the API’s high water solubility can lower the collapse temperature of the formulation, requiring conservative ramp rates and chamber pressure. After lyophilization, residual moisture is controlled by Karl Fischer titration to prevent hydrolysis in the sealed vial; vial headspace oxygen is reduced by nitrogen flushing because the oxacephem ring may undergo oxidative degradation. The stopper and seal configuration is selected to resist moisture ingress over shelf life; bromobutyl stoppers are common but require extractable and leachable assessment under USP <1663> and USP <1664>.
For oral tablet and capsule formulation, the same sodium salt is used, but the manufacturing train is generally non-sterile. The API is freely water-soluble and hygroscopic; therefore direct compression blends may exhibit sticking, picking, and variable tablet weight when tablet press tooling is not cooled or when relative humidity in the compression suite exceeds 60% RH. The sodium salt should be dispensed in a low-humidity suite and not held in open containers. Incompatibility with primary amines and strongly nucleophilic excipients should be assessed because β-lactam ring opening can produce inactive derivatives. Aqueous wet granulation is normally avoided unless simultaneous heat and moisture exposure is justified by stability data; dry granulation by roller compaction is preferred.
Granule and dry-syrup presentations require particle size control beyond simple sieve analysis. The API is often geometrically diluted with spray-dried lactose, mannitol, or microcrystalline cellulose in a bin blender of 100–1000 L working volume; blend uniformity is verified with thief sampling and analyzed by HPLC according to USP <905>. If a wet granulation step is unavoidable, non-aqueous binders or limited water addition with rapid drying in a fluid-bed dryer is used. The API should not be exposed to prolonged wet massing because sodium salt hydration and localized low pH can initiate hydrolytic degradation. Drying endpoint is controlled by near-infrared moisture probes calibrated against Karl Fischer; under-drying accelerates hydrolysis, while overdrying can increase static charge and reduce flowability. For capsules, the granulate is filled on automatic tamping or dosator machines that require controlled bulk density and flow function; hopper vibration and feed shoe overfilling are adjusted to prevent particle segregation.
Oral bioavailability of the sodium salt is constrained by ionization and acid-catalyzed degradation in the stomach; therefore an immediate-release oral tablet without enteric protection may show poor and variable absorption. If an enteric coating is applied, the coating level is critical: an incomplete coat exposes the API to gastric acid, while excessive coating delays release beyond the optimal absorption window. Dissolution testing is conducted using USP <711> apparatus 1 or 2, with acid-stage and buffer-stage media selected to demonstrate gastric resistance and intestinal release. Taste masking is also a requirement for pediatric granules and dry syrups. Coating of granules with ethylcellulose, methacrylic acid copolymers, or lipid matrices may be used, but the coating must not contain reactive amine plasticizers that can accelerate β-lactam ring opening. Stability under accelerated conditions at 40 °C/75% RH and long-term conditions at 25 °C/60% RH should include assay, related substances, dissolution, and moisture content; the sodium salt may show visible darkening before assay loss if headspace oxygen is not controlled.
The differentiation of Latamoxef Sodium from other β-lactam APIs is summarized in the comparison matrix below. The comparison is based on molecular properties and typical processing constraints, not on clinical superiority or therapeutic substitution.
| API class | Nucleus feature | Anaerobic spectrum | Key formulation constraint |
|---|---|---|---|
| Latamoxef Sodium | Oxacephem; 7α-methoxy; NMTT side chain | Bacteroides fragilis including some β-lactamase producers | Hygroscopic sodium salt; aseptic fill for injection; bleeding risk monitoring |
| Ceftriaxone Sodium | Cephalosporin; aminothiazolyl oxime | Limited anaerobic coverage | Incompatible with calcium-containing solutions in some parenteral contexts |
| Cefotaxime Sodium | Cephalosporin; aminothiazolyl oxime | Limited anaerobic coverage | Solution instability; dry powder or lyophilized presentation required |
| Meropenem Trihydrate | Carbapenem | Broad anaerobic coverage | Shorter reconstituted solution stability; cold-chain reconstitution required |
Process analytical technology on production lines can link near-infrared moisture measurements, particle size data, and HPLC impurity data to control batch-to-batch variability. In injectable filling, the dissolved API is filtered through sterile hydrophilic PVDF or PES membranes; the membrane manufacturer’s chemical compatibility data should be required because the sodium salt alters ionic strength and may change filter flux. Adsorption losses on nylon filters should be evaluated during filtration validation, and the final filling solution is sampled for bioburden before sterilizing-grade filtration. The constituted solution should be checked for pH, color, clarity, and reconstitution time because visible particulate formation in the presence of residual moisture or incompatible closure coatings is a known failure mode on production lines handling hygroscopic β-lactam sodium salts.