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Interferon Alfa 2b Effervescent Tablets Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Interferon Alfa 2b Effervescent Tablets Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 140705
    Productname Interferon Alfa 2b Effervescent Tablets Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Activeingredient Interferon Alfa-2b
    Casnumber 99210-65-8
    Molecularweight Approximately 19,271 Da
    Aminoacidcount 165
    Expressionsystem Recombinant Escherichia coli
    Appearance White to off-white powder
    Solubility Soluble in water and aqueous buffers
    Purity Typically >= 98% by HPLC
    Grade Pharma Grade
    Specificactivity Approximately 2.0 x 10^8 IU/mg
    Dosageforms Effervescent tablet, tablet, capsule, granule, injection
    Routesofadministration Oral and injectable
    Storageconditions Store at 2-8°C, protected from light, avoid repeated freeze-thaw
    Mechanismofaction Binds type I interferon receptor and activates JAK-STAT signaling
    Targetreceptor IFNAR1 and IFNAR2
    Halflife Approximately 2-3 hours after injection
    Atccode L03AB05
    Pharmacopoeiacompliance Complies with relevant pharmacopoeial standards where applicable
    Packaging Sealed sterile vial or container

    As an accredited Interferon Alfa 2b Effervescent Tablets 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 & Storage
    Packing 1 kg double-lined aluminum foil bag in a fiber drum, moisture-proof, light-resistant, sealed for pharma-grade interferon alfa-2b API.
    Container Loading (20′ FCL) 20′ FCL securely loaded with palletized Interferon Alfa 2b effervescent tablets, pharma-grade API, for oral/injectable use, ensuring stability and compliance.
    Shipping Interferon Alfa 2b Pharma Grade API ships under validated cold-chain conditions at 2–8°C, protected from light, moisture, and freezing. Use insulated, tamper-evident packaging with refrigerant packs, temperature loggers, and desiccants. Handle under GDP with proper labels, SDS, and customs documentation for oral/injectable pharmaceutical use.
    Storage Store Interferon Alfa 2b API in a tightly closed, light-resistant container under refrigeration at 2–8°C (36–46°F). Do not freeze. Protect from moisture, heat, and direct sunlight. Keep away from incompatible materials. Maintain cold-chain conditions for tablet, capsule, granule, oral, and injectable use. Store in original packaging; avoid temperature fluctuations. Follow manufacturer’s labeling and GDP/GMP requirements.
    Shelf Life Shelf life typically 24 months when stored sealed, cool, dry, and protected from light; reconstituted solutions are shorter and require refrigeration.
    Application of Interferon Alfa 2b Effervescent Tablets Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    In a Grade A aseptic filling line operating at 0.45 m/s unidirectional airflow inside an ISO 14644-1 ISO 5 cleanroom, interferon alfa 2b pharma grade API with a specific activity of 2.6 × 10^8 IU/mg is compounded into a lyophilized injection intermediate. The process is governed by ICH Q5A viral safety assurance, ICH Q5B genetic stability expectations, and ICH Q6B specification setting, together with release testing under Ph. Eur. 2.6.1 for sterility, Ph. Eur. 2.6.14 for bacterial endotoxins, USP <71>, USP <85>, and USP <790> for visible particulates. The liquid fill formulation is targeted at 10.0 × 10^6 IU/mL, corresponding to 38.5 µg/mL of active cytokine mass at the stated specific activity; excipients may include glycine or mannitol as a bulking agent, a 10 mM–25 mM sodium phosphate buffer at pH 7.0, and polysorbate 80 at 0.05 mg/mL–0.1 mg/mL depending on container closure and stability data. Bulk API is thawed, pooled, and buffer-exchanged by tangential flow filtration, then aseptically filtered through a 0.22 µm PVDF membrane and filled into Type I borosilicate glass vials. Lyophilization cycle development uses freeze-dry microscopy and product resistance data; a representative cycle includes shelf ramping at +0.3°C/min to -45°C, an annealing step near -10°C to reduce cake heterogeneity, primary drying at -20°C and 80 mTorr, and secondary drying at 25°C until Karl Fischer moisture per Ph. Eur. 2.5.12 reaches a release limit of ≤3.0% w/w. Stoppers are inserted under partial vacuum and aluminium caps are applied. The terminal finished product is a sterile lyophilized cake in a single-dose Type I glass vial for reconstitution with Sterile Water for Injection before subcutaneous, intramuscular, or intravenous administration. Batch-to-batch variance in cake appearance is most frequently traced to stopper moisture control; stopper moisture content above 0.5% before placement can cause local cake collapse and elevated residual moisture after accelerated stability storage.

    Quality attributeAnalytical method / standardTypical release criterion
    PotencyUSP Interferon alfa-2b monograph / Ph. Eur. 111080%–125% of label claim
    SterilityUSP <71>, Ph. Eur. 2.6.1No microbial growth
    Bacterial endotoxinsUSP <85>, Ph. Eur. 2.6.14Product-specific, commonly ≤5.0 EU/dose
    Subvisible particulate matterUSP <787>, Ph. Eur. 2.9.19≥10 µm ≤ 6000/container; ≥25 µm ≤ 600/container
    Residual moisturePh. Eur. 2.5.12≤3.0% w/w

    What Limits Subvisible Particle Counts in Liquid Injectable Interferon Alfa 2b?

    Liquid injectable presentations of interferon alfa 2b in prefilled syringes and cartridges are constrained by protein aggregation at silicone oil–water interfaces and by shear forces during filling. Compounding is performed in 316L stainless steel vessels under a nitrogen overlay; the API is added to a final concentration of 6.0 × 10^6 IU/mL to 30.0 × 10^6 IU/mL, equivalent to 23.1 µg/mL to 115.4 µg/mL at 2.6 × 10^8 IU/mg. A 10 mM–25 mM sodium phosphate buffer at pH 7.0 and polysorbate 80 at 0.05 mg/mL–0.1 mg/mL reduce aggregation during compounding, filtration, and storage. The solution is aseptically filtered through a 0.22 µm PVDF membrane and filled into pre-sterilized Type I glass prefilled syringes or cartridges. Production-scale filling lines show that peristaltic pump pulsation and high-shear filling nozzles can increase subvisible particle counts in the ≥10 µm and ≥25 µm channels; low-pulsation ceramic pumps and silicone-free or low-silicone container systems are therefore used where particle release limits are stringent. Finished product testing follows 21 CFR 211.165, with aseptic process validation under 21 CFR 211.113(b) and ISO 13408-1; particulate testing uses USP <787> and Ph. Eur. 2.9.19, with limits of ≤6000 particles per container at ≥10 µm and ≤600 particles per container at ≥25 µm for volumes ≤100 mL. The terminal finished product types are single-dose prefilled syringes and injector cartridges for subcutaneous injection. These products are stored at 2–8°C and are not terminally sterilized; prolonged exposure to temperatures above 40°C accelerates loss of potency and aggregate formation.

    When effervescent granulation is selected for an acid-labile 19.3 kDa cytokine, the primary process conflict is between the anhydrous processing required to protect interferon alfa 2b and the hygroscopic nature of the citric acid–sodium bicarbonate effervescent couple. A formulation protocol targeting 100,000 IU per tablet requires only 0.385 µg of API per tablet at a specific activity of 2.6 × 10^8 IU/mg; for a 2000 mg effervescent tablet, the API weight fraction is 1.9 × 10^-7 w/w. Direct addition is therefore impossible, and the API is first geometrically diluted with spray-dried mannitol at a 1:100 or 1:1000 ratio in a low-humidity glove box. The effervescent matrix is composed of anhydrous citric acid and sodium bicarbonate balanced to produce a solution pH of 5.5–6.0 after disintegration in 200 mL water; the exact acid-to-carbonate ratio is product-specific because the target pH governs available buffering capacity. Processing is dry: a 500 L V-blender operated at ≤25% RH mixes the API premix, acid, carbonate, and a binder such as PEG 6000, followed by direct compression on a rotary tablet press with chilled punches to prevent surface melting. Water-based wet granulation is avoided because it initiates premature effervescence and exposes the cytokine to acidic microenvironments. In-process controls follow 21 CFR 211.110; finished tablet testing includes Ph. Eur. 2.9.1 disintegration, Ph. Eur. 2.9.5 uniformity of mass, Ph. Eur. 2.9.7 crushing resistance, and USP <711> dissolution as a product-specific method. Stability is assessed under ICH Q1A(R2). The terminal finished product type is an effervescent tablet sealed in a cold-form aluminium foil blister with desiccant, or an effervescent granule in a single-dose sachet filled from the same dry blend; both are intended for reconstitution as an oral solution. Pack water activity is maintained below 0.4; lidding foil water vapour transmission rate is verified by ASTM F1249. Published commercial stability data for this specific oral effervescent configuration is limited; therefore, the API premix ratio, packaging moisture ingress, and disintegration pH must be validated on the actual production line before release.

    If Capsule Fill Weight Is Constrained Below 180 mg for Low-Dose Oral Immunomodulation Protocols

    For clinical protocols evaluating low-dose oral interferon alfa 2b in hydroxypropyl methylcellulose capsules, the API loading is constrained by fill accuracy and content uniformity rather than bulk manufacturability. A 50,000 IU capsule dose corresponds to 0.192 µg of API at 2.6 × 10^8 IU/mg, so the API is first dispersed into mannitol at 1:1000 w/w and then blended with silicified microcrystalline cellulose and sodium stearyl fumarate to a total fill weight of 120 mg. Blending is performed in a low-shear tumble mixer under ≤30% RH; HPMC capsule shells are conditioned to 10%–15% water content to avoid brittle fracture on the dosator-type encapsulation machine, which is operated with fill weight control at ±3.0%. Compliance testing includes Ph. Eur. 2.9.5 content uniformity and 21 CFR 211.165 finished product release; stability follows ICH Q1A(R2). The terminal finished product type is a hard HPMC capsule containing a dry powder blend for oral administration. Because published pharmacokinetic data for this specific oral interferon alfa 2b capsule configuration is limited, release is controlled by protocol-specific dissolution and content uniformity limits rather than a monograph-defined specification.

    Intralesional Injection Solution for Condyloma Acuminatum and Melanoma

    Intralesional injection solution presents interferon alfa 2b at a concentration of 10.0 × 10^6 IU/mL, equivalent to 38.5 µg/mL at 2.6 × 10^8 IU/mg, in a sterile liquid formulation filled at 1.0 mL per Type I glass vial. The manufacturing route—compounding, 0.22 µm aseptic filtration, and filling under unidirectional airflow—mirrors liquid injectable processing but must comply with USP <71>, USP <85>, Ph. Eur. 2.6.1, and Ph. Eur. 2.6.14. Multi-dose presentations require preservative efficacy testing under USP <51>; the preservative type and concentration are product-specific. The terminal finished product type is a single-dose or multi-dose vial for intralesional injection in condyloma acuminatum and melanoma protocols. Freezing is an operational boundary: repeated freeze-thaw cycles generate soluble and insoluble aggregates that raise subvisible particle counts beyond USP <787> limits.

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    Certification & Compliance
    More Introduction

    The product identified as Interferon Alfa 2b Effervescent Tablets Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a recombinant human interferon alpha-2b drug substance supplied for downstream formulation into multiple presentations. The molecule is expressed in Escherichia coli as a non-glycosylated polypeptide of 165 amino acid residues, with two intrachain disulfide bonds located at Cys1–Cys98 and Cys29–Cys138, and a calculated molecular mass of 19,271 Da. Because the host is a prokaryote, the product lacks the O-linked and N-linked glycan structures present in mammalian-cell-derived interferon alpha preparations. This absence of glycosylation alters hydrodynamic behavior, susceptibility to aggregation, and clearance, but does not remove the receptor-binding domain for IFNAR1 and IFNAR2. Potency is assigned by antiviral activity against the World Health Organization international standard for interferon alfa-2b and is expressed in international units per milligram of protein. Parenteral-grade release material is ordinarily controlled to not less than 1.0×108 IU/mg protein, with the assigned value reported on a batch-specific certificate of analysis.

    Pharmaceutical-grade status indicates manufacture under ICH Q7, EU GMP Annex 2, and applicable sections of 21 CFR 210/211, with viral safety assurance based on ICH Q5A, cell-substrate documentation under ICH Q5D, and specification design under ICH Q6B. Residual host-cell protein, host-cell DNA, endotoxin, and bioburden are not fixed identically for all presentations; the maximum tolerated values depend on whether the API is intended for injection, capsule, tablet, granule, or effervescent solid oral use. The title should be read as a formulation-capable API designation, not as a finished tablet. The active ingredient is supplied to a dosage-form manufacturer, which then introduces the protein into acid-base effervescent matrices, dry blends, granules, or sterile injectable formulations under conditions that must be qualified separately.

    What Distinguishes Interferon Alfa-2b from Interferon Alfa-2a and Pegylated Interferon Alfa-2b?

    At residue 23 of the mature polypeptide, interferon alfa-2b contains arginine, whereas interferon alfa-2a contains lysine. The remaining primary sequences are identical. Both alfa-2a and alfa-2b are produced in E. coli and are therefore non-glycosylated. Mammalian-cell-expressed interferon alfa subtypes, by contrast, carry glycan decoration that can reduce aggregation propensity, change net charge, and prolong circulating half-life. Pegylation of interferon alfa-2b attaches a monomethoxy polyethylene glycol moiety to the protein surface, increasing hydrodynamic radius and reducing renal clearance. Published pharmacokinetic data after subcutaneous administration of unpegylated interferon alfa-2b indicate an elimination half-life generally in the range of 2–8 h, while pegylated interferon alfa-2b exhibits a terminal half-life near 40 h. The distinction is therapeutically relevant because the unpegylated protein requires more frequent administration and may be more vulnerable to proteolytic loss if delivered by the oral route.

    Parameter Interferon alfa-2b Interferon alfa-2a Peginterferon alfa-2b
    Residue 23 Arginine Lysine Arginine with PEG attachment
    Glycosylation None None None
    Molecular mass 19,271 Da 19,241 Da Polydisperse, gravimetric mass increases with PEG
    Terminal half-life 2–8 h Similar to alfa-2b Approximately 40 h
    Primary route Injection; oral effervescent delivery remains investigational Injection Injection

    Release Specifications and Stability Boundaries Across Oral Solid and Parenteral Grades

    Release criteria for parenteral-grade interferon alfa-2b differ from those applied to tablet, capsule, and granule grades. Injectable material is controlled for sterility by membrane filtration according to Ph. Eur. 2.6.1 or USP <71>, and for subvisible particulate matter by light obscuration using Ph. Eur. 2.9.19 or USP <788>. Compendial limits for large-volume parenterals are not necessarily identical to those for small-volume protein injections, but the standard acceptance thresholds of 6000 particles per container at ≥10 µm and 600 particles per container at ≥25 µm are frequently applied for reconstituted injectable solutions. Bacterial endotoxin is tested by limulus amebocyte lysate methods under Ph. Eur. 2.6.14 or USP <85>, with the limit calculated from the maximum intended injectable dose according to Ph. Eur. 5.1.10 or USP <85>. Solid oral grades are controlled by microbial enumeration using Ph. Eur. 5.1.4 or USP <61>/<62>, with typical acceptance criteria for non-sterile oral preparations at not more than 102 CFU/g total aerobic microbial count and not more than 101 CFU/g total yeast and mold count. Water content is not a universal parameter; for a protein-containing granule it may be specified below 5.0% loss on drying, while the acid-carbonate effervescent base is usually required to remain below 0.5% free moisture to avoid premature carbon dioxide generation during processing and storage.

    Grade Critical parameter Representative control or method
    Parenteral API Specific activity ≥1.0×108 IU/mg protein by antiviral assay
    Parenteral API Bacterial endotoxin Dose-based limit per Ph. Eur. 5.1.10 / USP <85>
    Parenteral API Sterility No growth, Ph. Eur. 2.6.1 / USP <71>
    Parenteral API Subvisible particles USP <788> / Ph. Eur. 2.9.19
    Oral solid grade Total aerobic microbial count ≤100 CFU/g per Ph. Eur. 5.1.4 / USP <61>
    Oral solid grade Total yeast and mold count ≤10 CFU/g per Ph. Eur. 5.1.4 / USP <62>
    Effervescent base Free moisture <0.5% loss on drying in many effervescent systems

    When Effervescent Granulation Imposes Acid-Base and Moisture Constraints on Protein APIs

    Effervescent tablet manufacture combines an acid, typically anhydrous citric acid or tartaric acid, with a carbonate source such as sodium bicarbonate or sodium carbonate. Upon contact with water, the reaction releases carbon dioxide and produces a buffered solution; the initial local pH can fall below 4.0 before neutralization is complete. Interferon alfa-2b is most stable in aqueous formulations between pH 6.8 and 7.4, and acid exposure can induce unfolding, deamidation, and covalent aggregation. The stoichiometry of the acid-base couple also matters: one mole of anhydrous citric acid can react with 3 moles of sodium bicarbonate to generate 3 moles of carbon dioxide, so even small amounts of free moisture can initiate effervescence and increase tablet porosity during storage. For this reason the protein is preferably isolated from the effervescent couple in a separate granule, or dry-blended under strictly controlled humidity.

    Granulators handling the protein-containing fraction should operate with inlet air dew point not exceeding 5°C and relative humidity below 20%. Fluid-bed top-spray granulation with an aqueous binder exposes the protein to water for the duration of drying; if inlet temperature exceeds 40°C, thermal unfolding may accelerate. Dry granulation by slugging or roller compaction reduces moisture and thermal load but introduces shear stress at the compaction zone. Rotary tablet presses used for effervescent formulations should be equipped with external lubrication to avoid overmixing of magnesium stearate, and compression force is typically maintained between 10 kN and 20 kN to produce tablet hardness below 60 N as measured by USP <1217>. These conditions balance sufficient mechanical strength against rapid disintegration. High compaction pressure and long dwell time can collapse the porous structure required for effervescent tablets and can increase protein particle surface contact, favoring aggregation during storage.

    Lyophilization and Spray Drying Alter the Solid-State Conformation of Interferon Alfa-2b

    Parenteral-grade interferon alfa-2b is often supplied as a lyophilized cake from a buffered solution containing sodium phosphate, glycine, or trehalose as a stabilizer. Lyophilization embeds the protein in an amorphous matrix; residual moisture after lyophilization is conventionally specified at or below 2.0%. Spray drying for oral solid grades creates particles with high surface area and may introduce shear and air-water interface stress. If inlet temperature is above 60°C, surface denaturation and aggregate formation can occur even when the outlet temperature remains below the measured unfolding temperature of the protein. Trehalose or sucrose is preferred as a lyoprotectant for both lyophilized injection-grade and spray-dried oral-grade material. Reducing sugars such as glucose or maltose must be excluded because their aldehyde groups can undergo Maillard reactions with lysine residues of the protein, reducing potency and generating covalent adducts.

    Although the product title includes oral and injectable routes, oral administration of unmodified interferon alfa-2b is constrained by proteolytic degradation in the gastrointestinal tract and by negligible passive permeation across the intestinal epithelium. An effervescent tablet can deliver the protein into a buffered solution and may provide brief residence in the oral cavity, but it does not eliminate enzymatic hydrolysis in the stomach and small intestine. Published data for this specific oral effervescent configuration is limited; injectable presentations remain the route for which the pharmacokinetics and pharmacodynamics of interferon alfa-2b are most extensively characterized. Differences from other interferon products therefore arise at three levels: primary sequence variation at residue 23 compared with alfa-2a, absence of glycan decoration compared with mammalian cell-expressed interferons, and attachment of polyethylene glycol in pegylated forms. Each difference influences immunogenicity, receptor occupancy, elimination, and the selection of formulation stabilizers.

    Incompatibilities relevant to the API include strong oxidizing agents, alkaline conditions above pH 9.0, and prolonged exposure to silicone oil from prefilled syringe components. For solid oral manufacture, the API should not be dry-mixed with acidic components in the presence of free water, and product-contact surfaces should be passivated stainless steel to reduce metal-ion-catalyzed oxidation of methionine residues. Batch-to-batch variance in host-cell protein levels and aggregate content is controlled by process validation under ICH Q5A and ICH Q5E, but exact limits remain manufacturer-specific because the route of administration and maximum daily dose determine the permitted residual impurity load.

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