| HS Code | 238477 |
| Product Name | Meningococcal Polysaccharide Vaccine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Product Type | Bacterial polysaccharide vaccine antigen |
| Target Organism | Neisseria meningitidis |
| Target Serogroups | A, C, Y, W-135 |
| Molecular Weight | Varies by serogroup polysaccharide |
| Appearance | White to off-white powder or clear to slightly opalescent solution |
| Grade | Pharma Grade / API Grade |
| Purity | Typically ≥ 90% capsular polysaccharide |
| Solubility | Soluble in water; insoluble in organic solvents |
| Dosage Forms | Tablet, Capsule, Granule, Injection, Oral, Injectable |
| Route Of Administration | Oral and injectable |
| Shelf Life | Typically 24 months |
| Pharmacopoeia Compliance | USP, EP, BP, IP as applicable |
| Sterility | Sterile and non-pyrogenic for injectable use |
| Endotoxin Limit | ≤ 100 EU/mL or per pharmacopoeia |
| Packaging | Sterile vial, ampoule, blister, bottle, or sachet |
| Manufacturer | WHO-GMP certified manufacturers |
| Application | Active immunization against meningococcal disease |
As an accredited Meningococcal Polysaccharide Vaccine 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, sealed glass vials, 10 vials per carton, each with 5 mg Meningococcal Polysaccharide Vaccine Pharma Grade API for oral/injection use. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized Meningococcal Polysaccharide Vaccine Pharma Grade API drums, braced, temperature-controlled, for oral/injectable and solid dosage forms. |
| Shipping | Meningococcal polysaccharide vaccine API is shipped under strict cold-chain conditions at 2–8°C using validated insulated containers, temperature monitors, and gel packs. Classified as UN3373 Biological Substance, Category B, with compliant IATA/ADR packaging. Secure, tamper-evident, customs-documented. Avoid freezing; maintain stability from dispatch to delivery. |
| Storage | Store Meningococcal Polysaccharide Vaccine Pharma Grade API refrigerated at 2–8°C in a dry, well-ventilated area, protected from light and moisture. Keep containers tightly sealed, upright, and in original packaging. Do not freeze. Maintain sterile handling for injectable forms; avoid temperature fluctuations and contamination. Monitor storage temperature continuously and segregate from incompatible materials. Use first-in, first-out stock rotation. |
| Shelf Life | Stable typically 24–36 months under recommended refrigerated storage (2–8°C), protected from light and freeze-thaw cycles; confirm via supplier stability data. |
In conjugate bulk formulation, the purified meningococcal polysaccharide API is first size-reduced and activated for covalent conjugation to a carrier protein such as CRM197, diphtheria toxoid, or tetanus toxoid. The polysaccharide-to-protein ratio is not a fixed universal value. Licensed liquid quadrivalent conjugate presentations include 4 µg serogroup-specific polysaccharide per 0.5 mL dose conjugated to 48 µg diphtheria toxoid, and a co-packaged presentation containing 10 µg MenA oligosaccharide plus 5 µg each MenC, MenY, and MenW-135 conjugated to CRM197. After conjugation, unreacted polysaccharide, free carrier protein, and low-molecular-weight reaction by-products are removed by diafiltration or size-exclusion chromatography; the bulk is then exchanged into a pH 6.5–7.5 buffer system suitable for sterile filtration. Single-use tangential flow filtration cassettes are used to prevent cross-contamination between serogroup campaigns, and product retention is monitored by refractive index and total protein assay. The terminal bulk is a clear to slightly opalescent solution that must meet a bacterial endotoxin limit calculated from the maximum human dose per Ph. Eur. 2.6.14 and USP 85. This bulk is the common feedstock for ready-to-use liquid vials and lyophilized components, but the subsequent formulation diverges depending on serogroup stability and presentation format.
Aseptic filling of conjugate bulk after sterile filtration is carried out in an isolator or restricted access barrier system rated ISO 5 at working positions. The formulated bulk is passed through a 0.22 µm membrane filter qualified for bacterial retention according to ASTM F838-20; because high-molecular-weight polysaccharide conjugates can form shear-induced aggregates, the filter train is validated for product recovery and pressure decay. A multi-round filter sizing study is conducted when the bulk shows visible aggregates or rising differential pressure above 0.7 bar at the final membrane. Filling is performed by a rotary piston pump or peristaltic single-use pump into Type I borosilicate glass vials with nominal fill volume 0.5 mL. Stoppers are 13 mm chlorobutyl or bromobutyl elastomer components dried to residual moisture below 0.8% w/w before introduction to the line. Headspace oxygen is displaced by nitrogen overlay, and the vials are closed under Grade A air supply per EU GMP Annex 1 and ISO 14644-1 Class 5. The process includes in-process checks for fill weight, stopper seating depth, and container closure integrity by vacuum decay. The terminal product is a ready-to-use liquid injection stored at 2–8 °C, protected from light, with a shelf-life assigned from real-time stability data rather than accelerated data alone.
The lyophilized MenA component in a co-packaged quadrivalent presentation is not a simple freeze-dried antigen cake. Serogroup A polysaccharide formulated with sucrose or trehalose will form a heterogeneous ice structure if the freezing step is uncontrolled, producing a collapsed cake or slow reconstitution. Production cycles therefore insert an annealing hold at -15 °C to -20 °C for 2–4 h after the freezing ramp and before primary drying; the hold allows ice crystal ripening and increases the effective pore diameter in the dried matrix. Omission of annealing has been observed on production-scale freeze dryers as cake shrinkage from the vial wall, a defect that cannot be corrected by extending secondary drying. Primary drying is run at a shelf temperature no higher than -30 °C and chamber pressure between 50–150 µbar. Secondary drying at 25–35 °C lowers residual moisture to ≤ 2.5% w/w as measured by Karl Fischer titration per Ph. Eur. 2.5.12 or USP 921 Method Ia. The cycle is considered acceptable when the dried cake is white to off-white, reconstitutes in the liquid MenCWY component within 60 s, and shows no visible meltback under 2× magnification. The terminal product is a co-packaged vial set: one vial of lyophilized MenA conjugate and one vial of liquid MenCWY conjugate for intramuscular injection after reconstitution to 0.5 mL.
| Downstream operation | Standard designation | Technical control target |
|---|---|---|
| Sterile filtration membrane | ASTM F838-20 | 0.22 µm rated pore size |
| Fill-zone particulate environment | ISO 14644-1 | Class 5 at working position |
| Lyophilized cake moisture | Ph. Eur. 2.5.12 / USP 921 Method Ia | ≤ 2.5% w/w |
| Sterility release | Ph. Eur. 2.6.1 / USP 71 | No growth after incubation |
| Bacterial endotoxin release | Ph. Eur. 2.6.14 / USP 85 | Product-specific limit derived from maximum dose |
For oral enteric capsule prototypes, the API is dispersed in a non-reducing disaccharide matrix before wet granulation. A research formulation dilutes meningococcal polysaccharide antigen to 0.5–2.0% w/w of the granule dry mass, with trehalose or mannitol as filler, sodium citrate buffer to maintain pH 6.8–7.4 during rehydration, and polyvinylpyrrolidone K30 as binder at 2–5% w/w. The granulation is performed in a top-spray fluid-bed processor with inlet air temperature 45–55 °C, product temperature 28–32 °C, and atomising pressure 0.8–1.2 bar. Dried granules are sieved to 250–500 µm and filled into hydroxypropyl methylcellulose capsules of size 3. An enteric coating dispersion of methacrylic acid–ethyl acrylate copolymer is applied in a pan coater to a weight gain of 5–10% w/w. Triethyl citrate, when used as plasticizer at 10–20% w/w of polymer solids, alters film flexibility but can increase leachable surface residues; therefore the capsule shell is screened by LC-MS for plasticizer migration under 40 °C/75% RH stress. Acid resistance is tested by two-stage dissolution using USP 711 delayed-release apparatus: 0.1 N HCl for 2 h followed by phosphate buffer pH 6.8. Gastric protection does not by itself establish immunogenicity; the antigen must be characterized for O-acetyl retention, molar mass, and conjugate integrity after neutral pH exposure. Published data for this specific configuration are limited, and the prototype is not interchangeable with a licensed oral vaccine.
Tableting of unmodified meningococcal polysaccharide powder without co-processing generates compacts with tensile strength below 0.5 MPa at compaction pressures up to 150 MPa on an instrumented single-punch press. The freeze-dried or spray-dried antigen has poor plastic deformation and undergoes brittle fragmentation rather than forming strong interparticulate bonds. Addition of microcrystalline cellulose at 30–50% w/w, mannitol at 20–40% w/w, and crospovidone at 2–5% w/w brings the tensile strength into the range 1.2–2.0 MPa for oral research tablets. Capping is observed when the granule moisture falls below 1.0% w/w or when magnesium stearate is added before the filler is fully blended. Magnesium stearate is restricted to 0.5% w/w because higher amounts reduce compact breaking force and prolong disintegration beyond 15 min. Tablets are compressed to hardness 5–8 kp and friability below 1.0% per USP 1216. The terminal product is a research tablet used to evaluate antigen stability and release profiles in mucosal delivery models; it is not a licensed dosage form and requires separate demonstration of antigen identity and potency after compaction.
Granulated oral vaccine intermediates are prepared by twin-screw dry granulation instead of aqueous granulation when the O-acetyl content of serogroup A polysaccharide must be preserved. Loss of O-acetyl groups can occur during wet massing at pH above 8.0 or at temperatures above 40 °C for more than 2 h; therefore, dry granulation with a binder such as hydroxypropylcellulose at 3–6% w/w is used. The powder blend is compacted on a twin-screw granulator with screw speed 50–100 rpm and screen aperture 1.0 mm. The resulting granules are filled into capsules or compressed into tablets after blending with disintegrant. Process analytical technology is applied by near-infrared monitoring of antigen content uniformity and moisture below 2.0% w/w. The terminal product is an oral solid dose intermediate for preclinical immunogenicity studies; injectable product is not manufactured by this route.
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Meningococcal Polysaccharide Vaccine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a purified capsular polysaccharide intermediate derived from Neisseria meningitidis serogroups A, C, W135, and Y. The material is released as a bioburden-controlled or sterile lyophilized powder and as a concentrated aqueous bulk for downstream vaccine manufacture. The tablet, capsule, and granule descriptors are not equivalent to licensed oral vaccine presentations; they refer to the solid-state format of the bulk intermediate during formulation screening or to oral feasibility work. Unconjugated meningococcal polysaccharide is an injectable T-cell-independent antigen. Published data for oral efficacy of this unconjugated antigen are limited, and no oral bioavailability claim is made.
No global proprietary model code applies to the base-grade material. The product is specified by serogroup composition, molecular size distribution, O-acetyl content, residual protein, nucleic acid, bacterial endotoxin, sterility, and residual moisture. A manufacturer-specific code is assigned only after lyophilization into a defined container-closure system and after the batch dossier confirms compliance with the injectable grade release panel.
The material is used as the antigen drug substance for injectable meningococcal polysaccharide vaccines and as the starting polysaccharide for activation and conjugation in conjugate vaccine manufacture. For injectable formulation, the powder is reconstituted in phosphate-buffered saline and diluted to the final antigen concentration for sterile filling. The product is not interchangeable with conjugated MenACWY intermediates, whole-cell vaccines, or pneumococcal polysaccharide APIs.
The release specification is aligned with current WHO recommendations for meningococcal polysaccharide and conjugate vaccine production and with applicable European Pharmacopoeia general methods. Identity is confirmed by immunodiffusion or enzyme-linked immunosorbent assay with serogroup-specific antisera. Molecular size distribution is controlled by high-performance size-exclusion chromatography with refractive index detection. The acceptance criterion is expressed as a distribution coefficient relative to a serogroup-specific reference standard. O-acetyl content is measured by the Hestrin colorimetric reaction because de-O-acetylation of group C polysaccharide reduces recognition by serum bactericidal antibodies. Residual protein is determined by the Lowry method or Ph. Eur. 2.5.33. Nucleic acid is assessed by absorbance at 260 nm. Bacterial endotoxin is tested by Ph. Eur. 2.6.14 or USP <85>. Sterility is tested by membrane filtration per Ph. Eur. 2.6.1 or USP <71>.
| Attribute | Method or standard | Acceptance framework |
|---|---|---|
| Identity | Immunodiffusion or ELISA with group-specific antisera | Positive reaction at reference concentration |
| Molecular size distribution | HPSEC-RI | Distribution coefficient limit relative to reference standard |
| O-acetyl content | Hestrin colorimetric method | Serogroup-specific minimum set by marketing authorisation dossier |
| Residual protein | Ph. Eur. 2.5.33 / Lowry | NMT 1.0% w/w for purified polysaccharide bulk |
| Nucleic acid | UV absorbance at 260 nm | NMT 1.0% w/w for purified polysaccharide bulk |
| Bacterial endotoxin | Ph. Eur. 2.6.14 / USP <85> | Limit assigned per finished vaccine dose |
| Sterility | Ph. Eur. 2.6.1 / USP <71> | Compliant for injectable grade |
| Residual moisture | Karl Fischer Ph. Eur. 2.5.12 | NMT 3.0% for lyophilized powder |
Serogroup A polysaccharide contains N-acetylmannosamine-1-phosphate repeating units linked by phosphodiester bonds. This phosphodiester backbone is acid-labile. Serogroup C polysaccharide is a homopolymer of α-2,9-linked N-acetylneuraminic acid carrying O-acetyl groups. W135 and Y polysaccharides contain sialic acid alternating with galactose or glucose. These structural differences require serogroup-specific identity testing before pooling. A positive reaction outside the homologous serogroup indicates contamination or batch misassignment.
Depolymerization control is the main processing boundary for this API. For serogroup A, acid-catalysed hydrolysis of the phosphodiester linkage accelerates below pH 6.0. For serogroup C, de-O-acetylation and desialylation can occur under alkaline or high-temperature conditions. During purification, pH is maintained between 6.0 and 7.4, and process temperatures are held below 25 °C except during short controlled precipitation steps. Lyophilization is performed with an annealing step above the freeze-concentrate collapse temperature determined by freeze-drying microscopy. Chamber pressure is held below the critical collapse pressure. Without annealing, production-scale tray dryers show shrinkage and collapse at the bottom of the cake because product resistance slows sublimation. De-O-acetylation of group C polysaccharide follows pseudo-first-order kinetics in dilute acid; the Arrhenius activation energy should be determined for each serogroup because published data vary with counterion and ionic strength.
Commercial-scale purification uses jacketed stainless steel vessels with bottom-mounted low-shear impellers. Transfer lines are operated at minimal shear using positive displacement pumps rather than centrifugal pumps. Cavitation in centrifugal transfer has been observed to shift HPSEC-RI distribution beyond the reference standard limit. Depth filtration through cellulose-based media reduces endotoxin and bioburden before final filtration. For injectable grade, final sterilising filtration through a 0.22 µm polyvinylidene fluoride membrane is performed after bulk formulation. For dry powder intermediates, filtration occurs before lyophilization.
The plain polysaccharide API does not contain a carrier protein. In conjugated meningococcal vaccine production, the polysaccharide is first depolymerized and activated with cyanogen bromide or carbodiimide chemistry, then coupled to tetanus toxoid, diphtheria toxoid, or CRM197. The conjugated product requires additional release tests for free saccharide, saccharide-to-protein ratio, and carrier protein integrity. The plain API release panel remains focused on capsular identity, molecular size distribution, O-acetyl content, and residuals. The plain polysaccharide is not interchangeable with a conjugate intermediate in infant immunisation schedules because the plain form induces a T-cell-independent response with poor immunogenicity in children under 2 years of age and lacks a reliable booster response. This is a product-specific distinction, not a statement of clinical superiority.
| Attribute | Plain polysaccharide API | Conjugated MenACWY intermediate |
|---|---|---|
| Carrier protein | Absent | Tetanus toxoid, diphtheria toxoid, or CRM197 present |
| Activation chemistry | Not applicable | Cyanogen bromide or carbodiimide activation before coupling |
| Key release attributes | Identity, molecular size, O-acetyl, residuals | Free saccharide, saccharide-to-protein ratio, carrier protein integrity |
| Infant immunogenicity | T-cell-independent, poor below 2 years | T-cell-dependent, suitable for infant schedules |
| Booster response | Limited | Expected after booster dosing |
| Validated route | Injectable | Injectable |
Relative to Haemophilus influenzae type b polyribosylribitol phosphate, the meningococcal API is more acid-labile in serogroup A and more dependent on O-acetyl integrity in serogroup C. Relative to pneumococcal polysaccharide APIs, the meningococcal product comprises fewer serogroups and is formulated as a tetravalent A/C/W135/Y intermediate. Cross-substitution is not permitted because identity tests are serogroup-specific and the immunological targets are unrelated.
For solid dosage screening, the lyophilized polysaccharide API can be blended with mannitol and microcrystalline cellulose, but direct compression is limited by hygroscopicity and low bulk density. If capsule or granule intermediates are prepared, processing must occur in low-humidity suites with relative humidity below 30% and product temperature below 25 °C. Aqueous granulation is incompatible with the phosphodiester and O-acetyl stability of the antigen. Any oral delivery claim would require an enteric-coated platform and demonstration of antigen uptake at Peyer’s patches. Published data for this specific configuration is limited.
The lyophilized API is stored at −20 °C ± 5 °C in sealed Type I glass vials with bromobutyl rubber stoppers. Repeated freeze-thaw cycles of the aqueous bulk are not recommended because molecular size decreases and O-acetyl content may fall. The material is incompatible with cationic surfactants after final purification, with acidic buffers below pH 6.0, and with oxidising agents. For injectable formulation, phosphate-buffered saline at pH 6.5–7.4 is used. Calcium-containing diluents are avoided to prevent precipitation of phosphate salts.
Compliance for the injectable grade is demonstrated through a dossier referencing current WHO recommendations for meningococcal polysaccharide vaccines and the relevant Ph. Eur. general methods. Because the product title includes oral and tablet designations, the dossier must clearly separate the validated injectable application from any solid oral feasibility work. Release for pharmaceutical use is not granted solely on the basis of dry weight or identity; the full test panel is performed on each batch.