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Sialic acid ( N-Acetylneuraminic acid) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Sialic acid ( N-Acetylneuraminic acid) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 173866
    Product Name Sialic acid (N-Acetylneuraminic acid) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemical Name N-Acetylneuraminic acid
    Cas Number 131-48-6
    Molecular Formula C11H19NO9
    Molecular Weight 309.27 g/mol
    Appearance White to off-white crystalline powder
    Assay ≥98.0% (HPLC)
    Grade Pharma Grade API
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Solubility Soluble in water; slightly soluble in methanol and ethanol; practically insoluble in nonpolar organic solvents
    Storage Conditions Store in a tightly closed container in a cool, dry place; protect from light and moisture
    Shelf Life 24 months under recommended storage conditions
    Packaging Double polyethylene bags inside a fiber drum; injection grade supplied in sterile sealed containers
    Melting Point 185-187°C (decomposes)
    Ph 2.0-3.0 (1% aqueous solution)
    Loss On Drying ≤1.0%
    Heavy Metals ≤10 ppm
    Microbial Limits TAMC ≤1000 CFU/g; TYMC ≤100 CFU/g; absence of E. coli
    Optical Rotation -30° to -34° (c=1, water)

    As an accredited Sialic acid ( N-Acetylneuraminic acid) 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.

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    Application of Sialic acid ( N-Acetylneuraminic acid) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Sialic acid pharmaceutical-grade API is supplied as a white to off-white crystalline powder. The direct compression route is considered only after a pre-formulation screen confirms free moisture below 0.5% after drying at 40°C for 24 h. N-acetylneuraminic acid is a weak acid with pKa near 2.6, molecular weight 309.27 g/mol, and CAS registry number 131-48-6. The free carboxyl group contributes to punch filming when press feed-frame humidity exceeds 40% RH. Pilot-scale rotary compaction trials on a 16-station B-tooling press show that material with D50 below 45 µm creates die-fill variability above 3.0% RSD. A direct compression grade with D50 between 75 µm and 150 µm is therefore preferred for pharmaceutical tablet manufacture. The blend begins with a 1:1 pre-mix of sialic acid and mannitol. Microcrystalline cellulose is added to bring the API loading to 25–35 wt%. Crospovidone is used at 2.0–4.0 wt% to maintain disintegration performance. Magnesium stearate is added last at 0.5–1.0 wt% after the lubricant-free blend completes 150 rotations in a bin blender. Compression force is limited to 7–12 kN because tablets compressed above 12 kN show lamination under friability testing. Target tablet hardness is 60–90 N and friability is less than 1.0% by USP <1216>. Content uniformity is assessed by USP <905>. Dissolution is tested in 0.1 N HCl at 37°C with sampling at 15 min and 30 min. Published data for the dissolution specification of sialic acid immediate-release tablets is limited. Finished tablets are packed in aluminum-aluminum blisters because moisture uptake above 2.0% increases surface tackiness and slows disintegration. Elemental impurity risk is controlled according to ICH Q3D. Residual solvent levels are monitored by USP <467>. The terminal dosage form is an immediate-release oral tablet.

    What Happens When Sialic Acid Is Subjected to Wet Granulation?

    Aqueous wet granulation remains viable only within a narrow processing window. Sialic acid dissolves in water and creates solid bridges after drying. A binder solution of povidone K30 at 5 wt% concentration is introduced into the high-shear mixer. The binder amount is limited to 8–12% of dry granulate weight. Impeller speed is set at 150–200 rpm and chopper speed at 1000–1500 rpm. Wet massing time is limited to 20 min to prevent excessive solubilization and particle growth. Granule temperature is maintained below 45°C because sialic acid becomes discolored in hot acidic solution. The wet mass is passed through a 1.2 mm screen before drying. Drying is performed in a fluid-bed dryer with inlet air temperature at 55–65°C. Product temperature is kept below 40°C throughout the drying cycle. The endpoint is confirmed when loss on drying is below 2.0% by USP <921>. Dry granules are sized between 125 µm and 710 µm. Oversized granules are milled through a 0.8 mm screen at low speed. Wet granulation is not used when a fully crystalline API is required because partial amorphization increases hygroscopicity and lowers the glass transition of the dried granule. The final granules are stored with desiccant. The terminal dosage form is an oral tablet or granule. Published data for the long-term chemical stability of sialic acid wet granulations is limited.

    Capsule Filling Without Lactose

    Lactose-free capsule systems are selected to remove reducing-sugar interaction risk during stability. Sialic acid is filled into size 0 or size 1 capsules. Hard gelatin shells contain 13–16% water, which can transfer to sialic acid and cause powder caking. HPMC capsule shells with shell moisture below 7% are therefore preferred for moisture-sensitive sialic acid formulations. The capsule blend contains sialic acid at 40–60 wt%. A filler system of mannitol and pregelatinized starch in a 2:1 ratio is used to maintain flowability. Sodium stearyl fumarate is added at 1.0 wt% to replace magnesium stearate and reduce over-lubrication. Colloidal silicon dioxide at 0.5 wt% is pre-blended with sialic acid to reduce electrostatic adhesion to dosator surfaces. Filling is performed on an intermittent-motion capsule machine at 60,000 capsules/h. Tamping pin compression ratio is set to 1:1.2 to 1:1.4. Total fill weight for a size 0 capsule is 450 mg. Capsule weight variation is checked by USP <905>. Disintegration is tested by USP <701>. Relative humidity in the capsule filling suite is held at 25–30% RH. Final capsules are packed in HDPE bottles with heat-induction sealing and desiccant. Moisture ingress after 6 months is monitored by USP <921>. The terminal dosage form is an oral capsule.

    For injectable lyophilized powder, the API is dissolved in Water for Injection at 2–8°C. The solution pH is adjusted to 6.5–7.0 with 1 M NaOH. This converts the free acid to the sodium salt in situ and reduces precipitation risk. Mannitol is used as a bulking agent at 3.0–5.0% w/v. The solution is filtered through a 0.22 µm sterilizing-grade polyethersulfone filter. The filtrate is filled into 5 mL Type I glass vials at a fill volume of 2.0 mL. Vials are partially stoppered and loaded into the lyophilizer. The freezing step is performed at -40°C for 2 h. Primary drying is carried out at shelf temperature -20°C and chamber pressure 0.20 mbar for 24 h. Secondary drying is performed at 25°C for 6 h. The resulting cake is inspected for collapse and cracking. Collapsed or cracked cakes are rejected because incomplete sublimation leaves residual moisture that destabilizes the API. Lyophilized sialic acid is hygroscopic. Headspace moisture is controlled below 1.0% by Karl Fischer titration using USP <921>. The powder is reconstituted with 2.0 mL sterile water. Reconstitution time should be less than 60 s. Particulate matter is tested by USP <788>. Bacterial endotoxins are tested by USP <85>. Sterility is tested by USP <71>. The lyophilized product is intended for intravenous or intramuscular injection after reconstitution. Long-term stability is evaluated under ICH Q1A(R2) conditions. Published data for the long-term stability of sialic acid lyophilized cakes is limited.

    Dosage FormCritical Process VariableTarget RangeGoverning Standard
    Direct compression tabletCompression force7–12 kNUSP <1216>, USP <905>
    Hard capsuleBlend moisturebelow 2.0%USP <921>
    High-shear granuleProduct drying temperaturebelow 40°CUSP <921>
    Lyophilized injectionCake moisturebelow 1.0%USP <921>
    Liquid injectableOsmolality280–320 mOsm/kgUSP <785>

    When Terminal Sterilization Is Replaced by Aseptic Filtration

    When terminal sterilization is replaced by aseptic filtration, the manufacturing flow for liquid sialic acid injection must exclude any post-filtration heat step. The compounding vessel is jacketed and maintained at 5–10°C. The API is added slowly to WFI under nitrogen overlay. The solution pH is adjusted to 6.5±0.3 with sodium hydroxide. Mannitol is added to achieve final osmolality of 280–320 mOsm/kg. The solution is filtered through a 0.22 µm sterilizing-grade membrane. The filtrate is collected in a sterilized stainless-steel holding vessel. The hold time between sterile filtration and filling is limited to 4 h at 2–8°C. Aseptic filling is performed in an isolator or RABS classified as ISO 14644-1 Grade A. The fill volume is 2.0 mL or 5.0 mL per vial. In-line weight check is performed on 100% of filled units. The finished liquid product is stored at 2–8°C. Final specifications include pH 6.2–6.8, assay 95.0–105.0%, osmolality 280–320 mOsm/kg by USP <785>, particulate matter by USP <788>, bacterial endotoxins by USP <85>, and sterility by USP <71>. The terminal dosage form is a ready-to-use injectable solution.

    Granule Sachet Lines and Moisture Barrier Requirements

    Fluid-bed top-spray granulation is used for sialic acid stick-pack granules. The product bowl is charged with sialic acid, mannitol, and maltodextrin. Inlet air temperature is set to 60–65°C. Product temperature is maintained at 35–40°C. A spray solution of povidone K30 at 5 wt% is introduced at 8–12 g/min/kg of dry powder. Atomization air pressure is controlled between 1.2 bar and 1.8 bar. The resulting granules have a mean particle size of 200–300 µm. Drying continues in the same fluid-bed unit until loss on drying is below 1.5%. Cooled granules are screened through a 1.0 mm mesh. The final granulation is filled into stick packs made of polyester/aluminum foil/polyethylene laminate. Moisture vapor transmission rate is specified below 0.1 g/m²/day. This protects the sialic acid from humidity during storage. A horizontal form-fill-seal machine with auger filler is used. Fill weight is set between 1.0 g and 2.0 g per stick pack. Jaw sealing temperature is 160–180°C. Seal integrity is tested by vacuum leak at -0.6 bar for 3 min. The finished stick pack is an oral granule dosage form reconstituted in water before administration.

    Dose flexibility for pediatric or dysphagic patients requires an oral liquid. The solution is compounded with sialic acid in purified water at 5–25°C. The pH is adjusted to 5.5–6.5 with citrate buffer. This pH range minimizes free acid precipitation and reduces acid-catalyzed degradation. A preservative system of methylparaben and propylparaben is added only after pH adjustment to avoid ionization shifts. The bulk solution is filtered through a 0.45 µm clarifying filter. It is filled into amber glass bottles with child-resistant closures. Fill volume is 100 mL or 200 mL. The finished solution is stored at 2–8°C after first opening. Microbial limits are tested by USP <61> and USP <62>. Assay is performed by high-performance liquid chromatography with UV detection. The terminal dosage form is an oral liquid.

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    Certification & Compliance
    More Introduction

    The subject of this technical introduction is Sialic acid (N-acetylneuraminic acid) Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable. The chemical entity C11H19NO9, registered under CAS 131-48-6, is N-acetylneuraminic acid (Neu5Ac), a nine-carbon sialic acid supplied as a pharmaceutical-grade active pharmaceutical ingredient for oral and injectable dosage forms. The free acid has a molecular weight of 309.27 g/mol and an apparent carboxyl pKa near 2.6. The material is a white to off-white crystalline powder; it is freely soluble in water, and parenteral compounding is performed after neutralisation to pH 6.0–7.0 with sodium hydroxide. The API is manufactured under ICH Q7 GMP and is differentiated from food-grade or research-grade material by control of endotoxins, elemental impurities, residual solvents, and process-related impurities. The substance is intended as a raw material for tablets, capsules, granules, oral solutions, and injectable preparations; it is not supplied as a formulated drug product. Manufacturer-specific grade identifiers distinguish oral-grade material from injectable-grade material; the chemical entity is identical, but the injectable grade carries additional limits for bioburden, endotoxin, and particulate matter after reconstitution.

    Identity is confirmed by infrared absorption spectrophotometry according to Ph.Eur. 2.2.24 and by liquid chromatography retention time against a qualified reference standard. The specific rotation of the dried substance is measured at 589 nm and 20°C according to Ph.Eur. 2.2.7; lot-specific values are supplied in the certificate of analysis. Chiral purity and anomeric purity may be further characterised by 1H NMR and ion-mobility mass spectrometry; published data for this specific configuration is limited.

    What Release Specifications Differentiate Injectable-Grade Neu5Ac from Food-Grade Material?

    Because no harmonised pharmacopoeial monograph is published for N-acetylneuraminic acid, the release specification is manufacturer-specific and is established under ICH Q7 and ICH Q6A. The injectable grade adds bacterial endotoxin and particulate controls that are not applied to food-grade or cosmetic material. The following table lists typical release criteria for pharmaceutical-grade Neu5Ac; lot-specific certificates of analysis remain the authoritative source.

    AttributeAcceptance criterionMethod / standard
    AppearanceWhite to off-white crystalline powderVisual inspection
    Assay (dried basis)98.0%–102.0%HPLC, USP <621>
    Water content≤0.5%Karl Fischer titration, Ph.Eur. 2.5.12
    Related substancesTotal ≤1.0%; single ≤0.3%HPLC, Ph.Eur. 2.2.29
    N-glycolylneuraminic acid (Neu5Gc)Injectable ≤0.1%; oral ≤0.5%LC-MS/MS
    Bacterial endotoxinsInjectable <0.50 EU/mg; oral <2.0 EU/mgPh.Eur. 2.6.14, USP <85>
    BioburdenInjectable ≤10 CFU/g; oral ≤100 CFU/gPh.Eur. 2.6.12, USP <61>
    Residual solventsClass 1 not detected; Class 2 within ICH Q3C limitsICH Q3C, USP <467>
    Elemental impuritiesParenteral limits for injectable; oral limits for oralICH Q3D, USP <232>/<233>

    Dry powder stored in sealed double polyethylene bags bonded inside aluminium foil with desiccant at 2–8°C remains within release limits for up to 24 months under manufacturer stability protocols. Aqueous solutions of the free acid are not terminally sterilised because elevated temperature can induce pH-dependent de-N-acetylation and lactonisation; published data for this specific configuration is limited. Injectable processing therefore relies on aseptic filtration and controlled hold times at 2–8°C before lyophilisation or fill-finish.

    For tablet and capsule development, the free acid is commonly milled to a D90 below 75 µm and a D50 below 25 µm to support content uniformity in low-dose blends. Particle-size distribution is determined by laser diffraction according to ISO 13320-1:2020. The milled powder is hygroscopic; when relative humidity exceeds 60%, pre-drying in a vacuum tray dryer at 40–50°C for 2–4 h is required before blending. A final blend moisture content below 2.0% reduces sticking and particle agglomeration on tablet tooling. Flow assessment under USP <1174> typically classifies the milled free acid as cohesive; therefore dry granulation or roller compaction is preferred over direct compression for formulations exceeding 30% API load.

    When Dry Granulation Replaces Direct Compression for Low-Dose Tablet Formulations

    Roller compaction is selected when the API is poorly flowing and moisture-sensitive. Granules produced on a roller compactor at roll force sufficient to yield ribbon solid fraction of 0.6–0.7 and milled to a D50 between 150 µm and 250 µm provide a flowable intermediate for capsule filling and tablet compression. The process avoids high-shear wet granulation because the free acid’s carboxyl group interacts with water and binder polymers; residual granule moisture above 2.0% can initiate hydrate formation and reduce chemical stability. Published data for this specific configuration is limited, so formulators should run preformulation studies using differential scanning calorimetry and thermal analysis according to Ph.Eur. 2.2.34.

    Capsule filling and tablet compression are performed at 20–25°C and 40–50% RH. A pre-blend with mannitol or lactose monohydrate at 1:10 API-to-diluent ratio is prepared using a diffusion blender; subsequent lubricant addition of magnesium stearate is held below 1.0% because higher levels reduce tensile strength and delay disintegration. Tablet formulations compressed on a rotary tablet press with 8–18 kN force and hardness 60–120 N are typical starting targets, but published data for this specific configuration is limited and pilot-scale studies are required to confirm.

    In liquid formulations, the free acid is incompatible with amine-based buffers and strongly alkaline excipients because base-catalysed de-N-acetylation increases under pH >7.0. Lyophilised formulations should therefore avoid tromethamine and glycine buffers; citrate or acetate buffers at 5–25 mM and pH 5.5–6.5 are preferred for short-term stability. The dry powder should not be blended with alkaline lubricants such as sodium stearyl fumarate in high-moisture environments, because the local pH shift can promote degradation. Published data for this specific configuration is limited.

    Residual Impurity Control in Fermentation-Derived N-Acetylneuraminic Acid

    Fermentation-derived Neu5Ac differs from acid-hydrolysed edible bird’s nest fractions in process-related impurity control. The fermentation route can be controlled for host-cell proteins, DNA, endotoxin, and defined oligosaccharide by-products, whereas food-grade hydrolysates may contain variable glycoprotein fragments and are not manufactured under pharmaceutical GMP. Compared with N-glycolylneuraminic acid (Neu5Gc), N-acetylneuraminic acid is the predominant sialic acid in human glycans; Neu5Gc is generally controlled as an impurity because humans lack the CMAH enzyme and dietary incorporation of Neu5Gc can generate antibody-reactive glycoconjugates. Injectable-grade Neu5Ac therefore specifies Neu5Gc at ≤0.1%, whereas food-grade hydrolysates from animal sources may exceed this level and are not suitable for pharmaceutical use.

    AttributeInjectable pharma gradeOral pharma gradeFood-grade/research-grade
    Bacterial endotoxins<0.50 EU/mg<2.0 EU/mgNot specified
    Bioburden≤10 CFU/g≤100 CFU/gNot specified
    Neu5Gc≤0.1%≤0.5%May not be controlled
    Residual host-cell DNAControlled by qPCR batch releaseControlled, broader limitNot tested
    Elemental impuritiesICH Q3D parenteralICH Q3D oralNot tested
    Manufacturing standardICH Q7, EU GMP Annex 1 for injectableICH Q7Food GMP only

    The oral grade is suitable for tablets, capsules, granules, and oral solutions; the injectable grade is suitable for sterile liquid preparations and lyophilisates. The free acid is used when pH adjustment and buffer capacity are controlled at the formulation stage. The sodium salt of Neu5Ac may be selected for neutral-pH liquid formulations requiring faster dissolution; each gram of sodium Neu5Ac contains approximately 0.93 g free acid equivalent due to the difference in molecular weight. In contrast, food-grade material should not be substituted for pharmaceutical manufacture because endotoxin and impurity profiles are not validated for parenteral or oral drug products.

    Injectable compounding of the free acid is performed by dissolving the API in Water for Injection at 20–25°C, adjusting pH to 6.0–7.0 with sodium hydroxide, and adding sodium chloride to an osmolality of 280–320 mOsm/kg measured by USP <785>. The solution is passed through a 0.45 µm pre-filter and a 0.22 µm sterilising-grade polyethersulfone or polyvinylidene fluoride membrane under Grade A laminar airflow. Subvisible particulate matter in the filled product is controlled according to USP <788>: not more than 6000 particles per container at ≥10 µm and 600 particles at ≥25 µm for small-volume parenterals. Terminal steam sterilisation at 121°C for 15 min is not recommended for unbuffered solutions because pH drift and lactonisation may occur; aseptic filtration remains the primary sterilisation route. Published data for this specific configuration is limited, and hold-time studies at 2–8°C should be conducted before freeze-drying or terminal filling.

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