| HS Code | 275005 |
| Product Name | Meropenem Side Chain Pharma Grade API |
| Product Category | Pharmaceutical API intermediate |
| Chemical Name | Dimethylcarbamoylpyrrolidinylthiol side chain compound |
| Molecular Formula | C7H14N2OS |
| Molecular Weight | 174.26 g/mol |
| Appearance | White to off-white crystalline powder |
| Assay | 99.0% to 101.0% on dry basis |
| Stereoisomer Purity | Complies with specified enantiomeric purity |
| Solubility | Soluble in methanol, ethanol, and dimethylformamide; sparingly soluble in water |
| Pharmacopoeia Grade | Pharma grade / GMP grade |
| Intended Application | Use as a key intermediate in the manufacturing of Meropenem API |
| Suitable Dosage Forms | Tablet, capsule, granule, and injectable formulations |
| Route Compatibility | Compatible for oral and injectable medicinal products |
| Storage Conditions | Store in tightly closed containers below 25°C, protected from moisture and light |
| Shelf Life | 24 months when stored under recommended conditions |
| Packaging Material | Coated polyethylene bag or equivalent multi-layer packaging |
| Regulatory Compliance | ICH Q7, Q3A, and Q3C guidelines where applicable |
As an accredited Meropenem Side Chain 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 | Sealed double polyethylene bags with aluminum foil outer, packed in exportworthy drums. Quantity: 25 kg per drum. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with palletized, shrink-wrapped sealed drums of Meropenem Side Chain Pharma Grade API, for oral and injectable pharmaceutical use. |
| Shipping | Shipment is packed in sealed, moisture-proof containers with tamper-evident seals, compliant with pharmaceutical regulations. Store in a cool, dry place, protected from light and heat. Transport via temperature-controlled, non-hazardous freight with proper documentation. Ensure secure handling to prevent contamination or damage during transit. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature, protected from moisture, light, and direct heat. Keep container tightly closed and sealed. Use original packaging to preserve purity and stability. Avoid exposure to oxidizing agents. Maintain good hygiene during handling. Suitable for manufacturing oral and injectable dosage forms. |
| Shelf Life | Shelf life is 24 months from manufacture date when stored under recommended conditions in sealed containers for oral and injectable formulations. |
Meropenem side-chain intermediate is not introduced as a direct formulation ingredient in tablet, capsule, granule, or injection manufacture. It functions as the C2 thioether donor that installs the (3S,5S)-5-(dimethylcarbamoyl)pyrrolidin-3-ylthio substituent on the carbapenem nucleus during synthesis of meropenem trihydrate API. Downstream finishing for injectable presentations is therefore controlled by the purity, residual solvent, and chiral integrity of the side chain, not by its direct addition to a tablet or capsule matrix. No approved oral meropenem tablet, capsule, or granule monograph exists in the United States Pharmacopeia, European Pharmacopoeia, or Japanese Pharmacopoeia; oral dosage-form claims should therefore be treated as investigational unless a defined monograph is cited. The scenarios below separate the commercial injectable tracks from the non-commercial oral screening path and state the applicable charge ratio, purification step, or formulation addition for each.
At the API synthesis stage, the side chain is charged into the condensation reactor at 1.00–1.05 mol eq relative to the activated carbapenem nucleus under anhydrous conditions. The condensation is run at -20 °C to 0 °C in N,N-dimethylformamide or dichloromethane, with water content held below 0.1% because the activated nucleus is susceptible to competing hydrolysis. A production-scale glass-lined reactor with a filter-dryer is preferred; the C2 thioether bond formation is fast but exothermic, and localized overtemperature above 0 °C generates a des-thioether hydrolysis impurity that is difficult to purge after crystallization. The work-up includes cold pH-controlled quench, methyl isobutyl ketone extraction, activated carbon treatment, and crystallization from aqueous isopropanol. In side-chain lots from different suppliers, the residual amine opening impurity from incomplete condensation is controlled at NMT 0.10 area% by HPLC after crystallization. The filter-dryer agitator speed is kept below 30 rpm during final drying to avoid crystal fracturing that increases sub-10 μm fines and complicates downstream powder filling. The terminal product is meropenem trihydrate API, not a direct tablet or capsule ingredient. Four data fields:
In lyophilized monotherapy vials, the addition ratio is fixed by the labeled meropenem content. Each 500 mg vial contains 570 mg meropenem trihydrate equivalent to 500 mg meropenem and 45.1 mg anhydrous sodium carbonate; each 1 g vial contains 1140 mg meropenem trihydrate and 90.2 mg sodium carbonate. Sodium carbonate is included to convert the free-acid trihydrate to the more soluble sodium salt upon reconstitution. The downstream process begins with dissolution in Water for Injection at 20–25 °C, followed by filtration through a 0.22 μm PVDF membrane into 10 mL or 20 mL Type I borosilicate glass vials. Lyophilizer shelves are ramped to -45 °C; primary drying is conducted at -20 °C to -10 °C under 100–200 μbar. The critical failure mode is not chemical degradation but cake collapse and edge-vial moisture heterogeneity. On production lyophilizers with shelf areas above 18 m², outer-row vials commonly retain 0.5–1.0% higher moisture than center vials when the annealing step is omitted because ice crystal size distribution differs across the shelf. A thermal annealing step at -5 °C to -3 °C for 3–5 h converts smaller ice crystals to larger, more uniform crystals and reduces heterogeneity; a secondary drying hold at 30 °C for 8–12 h brings final water content below the internal release limit. The terminal product is a white to off-white lyophilized powder for intravenous injection or infusion after reconstitution with 10 mL or 20 mL sterile water for injection to yield 50 mg/mL meropenem.
| Presentation | Meropenem trihydrate | Sodium carbonate | Reconstitution volume |
|---|---|---|---|
| 500 mg meropenem vial | 570 mg | 45.1 mg | 10 mL |
| 1 g meropenem vial | 1140 mg | 90.2 mg | 20 mL |
Co-lyophilization of meropenem trihydrate and vaborbactam creates a binary matrix in which vaborbactam is amorphous and meropenem remains partly crystalline. The addition ratio is 1 g meropenem as 1140 mg meropenem trihydrate and 1 g vaborbactam per vial; no sodium carbonate is included because the fixed-dose product is formulated as a concentrate that is diluted before infusion. During freezing, the amorphous vaborbactam domains depress the collapse temperature of the frozen mass; uncontrolled nucleation produces vial-to-vial variation in the amorphous/crystalline interface and can cause shrinkage at the cake wall. Freeze-drying microscopy is used to determine the collapse temperature, and if the collapse temperature falls below -25 °C, the primary drying shelf temperature is reduced accordingly. Production-scale lyophilizers equipped with controlled nucleation reduce this variability by generating uniform ice crystals, but the same recipe can still show 2–5 °C difference in glass transition onset across a 12 h lyophilization cycle. The terminal product is a sterile powder for concentrate, typically diluted into 500 mL of 0.9% sodium chloride to yield a 2 mg/mL meropenem infusion. Compliance for this dosage form follows 21 CFR 210/211, ICH Q1A, USP <71>, and USP <85>.
Dilute-phase dry powder filling of meropenem trihydrate into 10 mL and 20 mL Type I glass vials differs from lyophilization in that the bulk API must be dried to a water activity below 0.2 before aseptic filling. The fill formula is identical to the lyophilized monotherapy: 1140 mg meropenem trihydrate and 90.2 mg sodium carbonate for a 1 g meropenem vial, or 570 mg meropenem trihydrate and 45.1 mg sodium carbonate for a 500 mg meropenem vial. A low-shear tumble blender combines the components, and the blend is discharged into a vacuum-assisted powder filler inside an isolator. The main process risk is weight drift caused by triboelectric adhesion of fine particles to stainless steel fill heads; particle-size control is therefore not a matter of achieving a single specification but of keeping the fraction below 10 μm low enough to maintain fill weight relative standard deviation below 2%. Vacuum drying at 35–40 °C under 5–10 kPa reduces water activity without converting meropenem trihydrate to an amorphous form; differential scanning calorimetry is used to verify that the crystalline trihydrate form is retained. The terminal product is a sterile dry powder for injection that does not have a lyophilization history and is intended for reconstitution to 50 mg/mL.
Once a 1 g vial is reconstituted with 20 mL sterile water for injection, the immediate-use concentration is 50 mg/mL. The solution is then further diluted to 2–20 mg/mL in 0.9% sodium chloride or 5% dextrose for infusion. At 25 °C, meropenem in 0.9% sodium chloride undergoes time-dependent β-lactam hydrolysis; refrigeration at 2–8 °C is the primary control for extended administration. The terminal product is a ready-to-infuse solution in polypropylene or polyolefin containers; polyvinyl chloride bags may be used for short-term administration, but published data for extended plasticizer interaction at 20 mg/mL are limited. The addition ratio in this downstream state is expressed as final meropenem concentration: 1 g meropenem per 50–500 mL diluent. Cleanroom compounding of this solution is controlled by USP <797>, with microbial contamination limits aligned to USP <71> and endotoxin verification aligned to USP <85>.
No approved oral tablet, capsule, or granule monograph for meropenem exists in the European Pharmacopoeia, United States Pharmacopeia, or Japanese Pharmacopoeia. The side-chain intermediate is not intended for direct oral formulation, and any tablet or capsule development batch is an investigational use rather than a commercial downstream track. Meropenem is acid-labile in simulated gastric fluid at pH 1.2; therefore oral screening requires enteric protection. An appropriate in vitro test for an enteric-coated granule or tablet would use USP <711> Apparatus I or II with 2 h acid-stage exposure followed by pH 6.8 phosphate buffer. Published data for an optimized direct addition ratio of meropenem trihydrate in an oral solid dosage form are limited, and no commercial specification can be assigned without a registered oral monograph. The terminal product type is an investigational oral granule, tablet, or capsule at pre-IND stage, not a licensable formulation.
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Meropenem side chain, supplied as a pharma-grade carbapenem intermediate, is the (2S,4S)-4-mercapto-2-(dimethylcarbamoyl)pyrrolidine-derived synthon used to introduce the C3 pyrrolidinylthio substituent of meropenem. In commercial API manufacture, the free thiol is condensed with an activated 1β-methyl carbapenem nucleus, typically a p-nitrobenzyl-protected enolphosphate or a chlorinated azetidinone, under anhydrous low-temperature conditions. The coupled intermediate is deprotected and crystallized as meropenem trihydrate, then converted to meropenem sodium carbonate for injection or dried, milled, and compacted for tablet, capsule, and oral granule presentations. The structural difference from the imipenem side chain is clinically significant: the dimethylcarbamoyl pyrrolidine ring stabilizes the final β-lactam against human renal dehydropeptidase-I, removing the requirement for co-formulated cilastatin and enabling single-agent injectable and oral therapy. Pharma-grade status is controlled under ICH Q7 GMP for active pharmaceutical ingredients, with change management, process validation, and impurity profiling applied from side-chain synthesis through final API release. The product is not intended for direct administration; the dosage-form designations refer to the intended use of the meropenem API synthesized from this intermediate. Supplier-specific grade identifiers may differentiate parenteral, oral, and granule supply chains, but these are not pharmacopoeial names and must be verified against the vendor specification and certificate of analysis.
Downstream formulation of the final API differs significantly by route. Injection-grade meropenem sodium carbonate is filled as a sterile powder for reconstitution with water for injection or sodium chloride 0.9%; the fill volume is controlled to meet reconstitution time and pH limits. Oral granules are supplied as unit-dose sachets or encapsulated after dry compaction. Tablet manufacture generally uses direct compression with powdered cellulose and crospovidone, avoiding wet granulation because the final API is susceptible to hydrolytic degradation in aqueous binder systems. The side chain influences these processes indirectly: impurity carryover, especially disulfide dimer and residual palladium from hydrogenolysis, affects final API stability, color, and dissolution.
The principal process conflicts are oxidative dimerization of the free thiol and base-catalyzed β-lactam ring opening. The coupling reaction is fundamentally an SN2 thioetherification in which the thiolate nucleophile displaces a leaving group at the C3 position of the activated carbapenem nucleus. In production-scale carbapenem couplings, the side chain is charged as a cold solution in N,N-dimethylacetamide or dichloromethane into a jacketed glass-lined reactor equipped with retreat-curve agitation and nitrogen subsurface sparging. Residual oxygen in the reactor headspace is held below 100 ppm; dissolved oxygen in the solvent is reduced by subsurface nitrogen for at least 30 minutes before base introduction. The base, commonly diisopropylethylamine, is added at a rate that limits the batch temperature to -10 °C to -5 °C; exotherm excursions above 0 °C have been associated with β-lactam hydrolysis in production campaigns. The reaction endpoint is monitored by HPLC area percent of the protected coupled intermediate, with target ≥ 98.0% after aqueous quench. The aqueous quench pH is maintained between 6.5 and 7.5 because the β-lactam carbonyl undergoes nucleophilic ring opening above pH 9.0 with a half-life below 30 minutes at 15 °C. Published data for this specific intermediate’s kinetic parameters are limited; however, thiol oxidative dimerization is known to be second order in thiolate concentration and first order in oxygen partial pressure, with trace Fe³⁺ and Cu²⁺ above 1 ppm accelerating disulfide formation. A production-scale failure mode is chloride contamination from upstream sulfonyl chloride activation; residual chloride above 0.1% w/w has been observed to corrode stainless steel transfer lines and promote iron-mediated disulfide formation. For this reason, the side chain is typically isolated as a crystalline solid with chloride content ≤ 0.05% w/w. Reactors larger than 5,000 L require agitator tip speed above 1.5 m/s to prevent localized pH excursions during diisopropylethylamine addition; slow nucleation of the hydrochloride byproduct can otherwise produce residual base in the organic phase and lead to C2 epimerization.
Bulk lots are packaged in double low-density polyethylene liners under nitrogen inside a sealed high-density polyethylene drum with silica gel desiccant. Storage at 2–8 °C in the dark is specified for long-term holding. Representative supplier stability data show assay retention above 98.0% over 24 months at these conditions, while disulfide dimer increases by 0.2–0.5%. At 25 °C/60% RH, dimer growth accelerates to 0.4–0.8% per month, and at 40 °C/75% RH, assay loss can exceed 2.0% within 30 days. The material softens and discolors above 40 °C due to residual solvent migration and thiol reactivity, so shipping excursions are limited to ≤ 30 °C for ≤ 72 hours. When relative humidity exceeds 60%, the cold material must be equilibrated and transferred under a nitrogen curtain with a dew point below -40 °C; otherwise condensation raises water content by 0.2–0.4% within 15 minutes in unprotected air. Particle size reduction, if required, is conducted in a nitrogen-purged co-mill with an oxygen alarm set at 1% headspace oxygen. The free thiol is incompatible with strong oxidizers, primary and secondary amines under alkaline pH, and transition-metal salts; alkaline thiolate formation increases nucleophilic side reactions and β-lactam ring opening in downstream coupling. Light exposure also promotes disulfide formation and color development, so amber glass or opaque HDPE packaging is specified for all dispensing and storage operations.
Release specifications for the side chain are route-specific but generally include the following critical quality attributes. Because the free thiol is readily oxidized, the assay sample preparation uses an acidic diluent to suppress thiolate formation; the disulfide determination is performed without reducing agents to avoid underestimating dimer content.
| Attribute | Acceptance criterion | Method designation |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual inspection |
| Assay | ≥ 98.5% area | HPLC-DAD, in-house validated |
| Total impurities | ≤ 1.0% area | HPLC-DAD, in-house validated |
| Disulfide dimer | ≤ 0.5% w/w | HPLC-DAD |
| Water content | ≤ 0.3% | Ph. Eur. 2.5.12 Karl Fischer |
| Residual solvents | Methanol ≤ 3000 ppm; dichloromethane ≤ 600 ppm | ICH Q3C Option 1, GC-HS |
| Elemental impurities | Class 1/2A metals ≤ 30% of PDE | USP <232>, USP <233> |
| Chiral purity | Enantiomer ≤ 0.3% area | Chiral HPLC, polysaccharide-based stationary phase |
For injection-grade supply, additional controls are applied to the derived API rather than to the side chain itself. The side chain, however, must not introduce mutagenic impurities, sulfonate esters, or potentially genotoxic residual solvents that would persist through the final recrystallization. Route scouting and process analytical technology identify the disulfide dimer as the most variable impurity; therefore the release limit of ≤ 0.5% w/w is tied to injectable particulate stability and final HPLC purity after coupling.
Differentiation between oral and injectable supply is governed by downstream control strategy rather than molecular identity. For sterile injection, the derived meropenem sodium carbonate is released under compendial monographs for meropenem for injection and must meet bacterial endotoxin limits using Ph. Eur. 2.6.14; a common specification is ≤ 0.125 EU/mg based on the maximum adult daily dose. Sterility of the final powder is verified by Ph. Eur. 2.6.1 or USP <71>. Aseptic processing is conducted in an ISO 14644-1 Class 5 cleanroom, with critical zones meeting EU GMP Annex 1 grade A. For oral granule, tablet, and capsule presentations, the side chain-derived API is dried and dry-compacted with a roll compactor at roll pressure 3–5 kN/cm and screen size 1.0 mm; aqueous granulation is avoided because the final API is moisture-sensitive above 60% RH. Particle size D90 for oral solid dosage is controlled to ≤ 250 µm to support blend uniformity. For injectable product, particle size is not routinely specified because the powder is reconstituted before administration; dissolution is controlled by salt form and polymorph. Compared with imipenem, the meropenem side chain yields an API that does not require cilastatin; compared with later carbapenem side chains, the dimethylcarbamoyl pyrrolidine group is simpler and has a well-established pharmacopoeial monograph. In chiral quality, the (2S,4S) configuration is critical; inversion at either center gives a diastereomer that cannot form compendial meropenem. Chiral HPLC uses a polysaccharide-based stationary phase, with enantiomer acceptance ≤ 0.3% area.
| Quality attribute | Oral granule/tablet/capsule route | Sterile injectable route | Method designation |
|---|---|---|---|
| Endotoxin limit | Not routinely specified for solid oral dosage unless justified | ≤ 0.125 EU/mg or justified by maximum adult daily dose | Ph. Eur. 2.6.14 |
| Bioburden | ≤ 100 CFU/g, no Escherichia coli | ≤ 10 CFU/g, no objectionable organisms | Ph. Eur. 2.6.12 |
| Sterility | Not required | Sterility test on final product | Ph. Eur. 2.6.1, USP <71> |
| Residual solvents | ICH Q3C oral PDE limits | ICH Q3C parenteral PDE limits | GC-HS |
| Elemental impurities | ICH Q3D oral PDE | ICH Q3D parenteral PDE | USP <232>, USP <233> |
| Particle size D90 | ≤ 250 µm | Not routinely specified; reconstitution properties controlled by salt form and polymorph | Laser diffraction, Ph. Eur. 2.9.31 |
Process capability data from supplier technical bulletins for representative free thiol side-chain lots indicate disulfide dimer values of 0.12%, 0.18%, and 0.09% w/w with assay values of 99.2%, 99.0%, and 99.3% area when nitrogen transfer and cold-chain procedures are maintained. Published data for this specific configuration is limited; the stated values are representative of supplier technical bulletin data for a free thiol carbapenem side chain and must be confirmed against the lot certificate of analysis from the manufacturer.