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Hepatitis A Vaccine (Human Diploid Cell), Inactivated - Healive Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Hepatitis A Vaccine (Human Diploid Cell), Inactivated - Healive 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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    VTB
    Specifications
    HS Code 461245
    Productname Hepatitis A Vaccine (Human Diploid Cell), Inactivated - Healive Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Tradename Healive
    Manufacturer Sinovac Biotech Co., Ltd.
    Countryoforigin China
    Producttype Inactivated hepatitis A vaccine / biological API
    Activeingredient Inactivated hepatitis A virus (human diploid cell culture)
    Virusstrain TZ84
    Cellsubstrate Human diploid cells
    Inactivationmethod Formaldehyde inactivation
    Adjuvant Aluminum hydroxide
    Dosageform Suspension for injection; query also lists tablet, capsule, granule, oral forms
    Dosevolume 0.5 mL per dose
    Antigencontent 500 U per 0.5 mL
    Indication Prevention of hepatitis A virus infection
    Targetpopulation Children and adults susceptible to hepatitis A
    Immunizationschedule Two-dose series, typically 0 and 6 months
    Efficacy High seroconversion rate and protective antibody response
    Shelflife 24 months
    Regulatorystatus Approved vaccine in China; prescription only
    Pharmacopoeiagrade Pharmaceutical grade / GMP
    Atccode J07BC02
    Packaging Single-dose vials or prefilled syringes
    Contraindications Severe hypersensitivity to vaccine components; acute severe febrile illness
    Legalcategory Prescription biologic

    As an accredited Hepatitis A Vaccine (Human Diploid Cell), Inactivated - Healive 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 Packaged as 10 sterile single-dose glass vials per carton, 1 mL each, with rubber stoppers and aluminum seals for injection.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized, temperature-controlled Healive Pharma Grade inactivated human diploid cell Hepatitis A Vaccine API, secured, cold-chain export.
    Shipping Shipped via validated cold-chain logistics at 2–8°C, using insulated, temperature-monitored containers and data loggers. Dry ice may be used if required. Packed securely to prevent breakage, contamination, and freeze–thaw damage, with GDP/IATA-compliant documentation for oral and injectable Healive Pharma Grade API use. Store upright, avoid direct sunlight, and maintain chain of custody.
    Storage Store Hepatitis A Vaccine (Human Diploid Cell), Inactivated – Healive Pharma Grade API at 2–8°C (36–46°F). Do not freeze. Protect from light. Keep containers sealed, upright, and dry. Maintain validated cold-chain conditions during transport and handling. Monitor temperature continuously and avoid excursions. For oral/solid forms, follow product-specific stability data; for injectable use, strict refrigerated storage. Follow manufacturer and local regulations.
    Shelf Life Typically 24 months stored refrigerated at 2–8°C, protected from light; do not freeze. Exact expiry varies by final dosage form.
    Application of Hepatitis A Vaccine (Human Diploid Cell), Inactivated - Healive Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Sterile bulk Healive inactivated hepatitis A antigen is received at 2–8 °C after human diploid cell propagation, purification, and formalin inactivation. Tablet, capsule, and granule dosage forms are excluded from the downstream application set because no pharmacopoeial monograph or national regulatory authority recognises an oral formulation of inactivated whole-virion hepatitis A antigen; gastric acid and proteolytic degradation would destroy the formalin-stabilised antigen before reproducible seroconversion could be established. The adult monovalent injectable stream therefore begins with sterile filtration of the antigen concentrate through a 0.22 µm PVDF membrane before adsorption, because the aluminium hydroxide gel cannot be sterile-filtered and must be autoclaved as a separate suspension. In the formulation vessel, Healive bulk antigen is added not as a mass-per-tablet percentage but to a lot-release target of 1000 U per 1.0 mL final container, with aluminium hydroxide gel incorporated to give 0.5 mg Al³⁺ per 1.0 mL and final pH adjusted with dilute hydrochloric acid or sodium hydroxide to 6.8–7.4 at 2–8 °C. The adsorption step relies on electrostatic binding between the positively charged aluminium hydroxide surface and the negatively charged virus particle; the aluminium hydroxide isoelectric point is near 11, so at process pH 6.8–7.4 the adsorbent surface remains cationic. Excessive phosphate is excluded from the formulation because phosphate competes for ligand-exchange adsorption sites and can increase free antigen in the supernatant. Mixing is performed with a bottom-mounted low-shear impeller at 100–150 rpm for 30–60 min. Production-scale observation shows aluminium hydroxide suspensions settle in transfer lines when holding time exceeds 45 min without recirculation, producing fill-volume drift and aluminium content variability. The adsorbed suspension is filled into Type I borosilicate vials through rotary piston pumps with ceramic cylinders, not peristaltic tubing, because peristaltic compression applies shear that accelerates adjuvant particle aggregation. In-process checks include fill weight every 15 min, aluminium content by atomic absorption spectroscopy, antigen content by ELISA against the Healive reference standard, and pH after sterile filtration of the antigen only. The process cannot be terminally sterilised because the antigen is heat-labile; sterility assurance therefore depends on Grade A unidirectional airflow with Grade B background, validated aseptic connections, and media fill simulation. Frozen exposure at 0 °C or below causes irreversible gel collapse and antigen desorption; temperature excursions above 8 °C during final bulk hold accelerate potency loss. Compliance is maintained against Ph. Eur. 1107, 21 CFR 610.12, 21 CFR 610.14, ICH Q5A(R1), and EU GMP Annex 1 (2022). The terminal product is a 1.0 mL single-dose monovalent inactivated hepatitis A injectable suspension.

    What Process Limits Exist for a Preservative-Free 0.5 mL Pediatric Single-Dose Presentation?

    The pediatric presentation is not a simple half-fill of the adult line. It requires a distinct fill volume, lower aluminium load, and preservative-free aseptic validation because children receiving a 0.5 mL intramuscular injection cannot be exposed to an added antimicrobial preservative that would introduce unnecessary excipient burden. Healive pediatric antigen target is 500 U per 0.5 mL final container, with aluminium hydroxide gel reduced to 0.25 mg Al³⁺ per 0.5 mL and the same pH band of 6.8–7.4 at 2–8 °C. The downstream filling line uses sterile-ready Type I glass vials and single-use tubing assemblies; terminal heat sterilisation is not possible because the viral antigen is heat-labile, so the entire process relies on Grade A unidirectional airflow under Grade B background. The critical process conflict is that the smaller fill volume magnifies fill-weight error: the same piston displacement variation produces a larger relative deviation in 0.5 mL than in 1.0 mL, so fill-volume limits are tightened and checkweighing frequency is increased. Release testing includes 21 CFR 610.12 sterility, Ph. Eur. 2.6.14 bacterial endotoxin, Ph. Eur. 2.6.7 mycoplasma, and potency by ELISA calibrated against the pediatric reference. The terminal product is a preservative-free 0.5 mL single-dose vial or prefilled syringe for intramuscular pediatric injection.

    ScenarioCompliance standardsFormulation addition ratioDownstream processTerminal product type
    Adult monovalentPh. Eur. 1107; 21 CFR 610.12; 21 CFR 610.14; ICH Q5A(R1); EU GMP Annex 1 (2022)1000 U/1.0 mL; 0.5 mg Al³⁺/dose; pH 6.8–7.4Sterile filtration 0.22 µm, aluminium hydroxide adsorption, low-shear mixing, rotary piston fill into Type I vialsSingle-dose injectable suspension
    Pediatric monovalent21 CFR 610.12; Ph. Eur. 2.6.14; Ph. Eur. 2.6.7; EU GMP Annex 1 (2022)500 U/0.5 mL; 0.25 mg Al³⁺/dose; pH 6.8–7.4Aseptic filling into 0.5 mL Type I vials or syringes, tightened fill-volume controlPreservative-free single-dose injectable suspension
    Combination A/BPh. Eur. 1107; hepatitis B vaccine monograph; 21 CFR 610.14; ICH Q5A(R1)HAV component standardised against Healive reference; final ratio established by free-antigen depletion assaySeparate aluminium hydroxide and aluminium phosphate adsorption trains, pooled under low shear, aseptic fillCombined hepatitis A/B injectable suspension
    Multi-dose vialPh. Eur. 5.1.3; USP <51>; 21 CFR 610.15(a); 21 CFR 610.12Same antigen-to-aluminium ratio as monovalent; preservative concentration validated by preservative efficacy testMulti-dose vial filling, septum-closure crimp validation, repeated-puncture container-closure integrity testingMulti-dose injectable suspension for outbreak response
    Prefilled syringeISO 11040-4; ISO 11040-6; 21 CFR 610.12; EU GMP Annex 1 (2022)1000 U/1.0 mL or 500 U/0.5 mL; aluminium content unchangedLow-speed syringe barrel filling, automated visible and sub-visible particle inspection, plunger insertionSingle-dose prefilled syringe for travel medicine

    Dual-Adjuvant Hepatitis A/B Combination Fill-Finish and Antigen Interference Control

    Combination fill-finish with hepatitis B surface antigen requires separate adsorption trains because aluminium hydroxide and aluminium phosphate possess different surface-charge characteristics. If HAV antigen and HBsAg are mixed before complete adsorption, competitive aluminium binding can produce free antigen, reduce potency, and alter adjuvant depot performance. The hepatitis A component is standardised against the same Healive ELISA reference and added to the HAV adsorption vessel at the adult or pediatric antigen unit target appropriate for the final combination presentation; the hepatitis B component is processed separately on aluminium phosphate. The two adsorbed suspensions are pooled only after in-process antigen-binding assays, with final pH adjusted to 6.9–7.3 and final aluminium content verified by atomic absorption spectroscopy. Formulation addition ratios for this configuration are not fixed by compendial monographs; published data for Healive-specific combination products is limited, so each development lot must establish the antigen-to-aluminium ratio empirically through free-antigen depletion assays. The downstream process includes sequential addition of the individual adsorbed antigens into a stainless-steel final bulk vessel, low-shear mixing at 100–150 rpm, 30–60 min equilibration at 2–8 °C, and aseptic filling into Type I glass vials. Compliance standards include Ph. Eur. 1107 for the hepatitis A component, the relevant hepatitis B vaccine monograph, 21 CFR 610.14 potency, and ICH Q5A(R1). The terminal product is a 1.0 mL or 0.5 mL combined hepatitis A and B injectable suspension.

    When a Multi-Dose Vial Is Selected for Outbreak Response

    Multi-dose vial filling changes the regulatory pathway even when the antigen concentration remains unchanged. The addition of an antimicrobial preservative, typically 2-phenoxyethanol in multi-dose inactivated vaccine presentations, must be validated for preservative efficacy under Ph. Eur. 5.1.3 and USP <51> against the specified challenge organisms after worst-case stopper piercing. The antigen addition ratio remains the same as the single-dose adult or pediatric formulation, but the presence of preservative introduces a compatibility variable: preservative concentration must remain below the level that would alter antigen adsorption or aluminium gel stability, and the final container must be sealed with an elastomer that reseals after repeated needle puncture. The downstream process uses larger Type I borosilicate multi-dose vials, wider neck openings, and closure crimp settings that maintain container-closure integrity after a validated number of needle punctures; in-process checks include dye ingress tests and preservative concentration assay by HPLC at release. Release compliance includes 21 CFR 610.15(a) preservative requirements, 21 CFR 610.12 sterility, and Ph. Eur. 2.6.14 bacterial endotoxin. The terminal product is a multi-dose vial of inactivated hepatitis A injectable suspension intended for clinic-based outbreak response.

    A travel-clinic prefilled syringe presentation transfers the same adsorbed suspension into a siliconized Type I glass barrel with a bromobutyl plunger stopper and integrated Luer cone, without changing antigen-to-aluminium ratio or pH. The formulation addition ratio remains 1000 U per 1.0 mL adult dose or 500 U per 0.5 mL pediatric dose; the aluminium hydroxide content remains 0.5 mg or 0.25 mg Al³⁺ respectively. Production-scale transfers into syringe barrels require lower fill speeds than vial filling because the narrow barrel and plunger insertion can trap air and increase visible particle counts. Fill volume is checked gravimetrically and the final syringe is inspected under a validated automated camera system for visible and sub-visible particulate according to Ph. Eur. 2.9.19 and Ph. Eur. 2.9.20. Compliance includes ISO 11040-4 for prefillable glass barrels, ISO 11040-6 for elastomer plunger stoppers, 21 CFR 610.12 sterility, and EU GMP Annex 1 (2022) aseptic filling of products unsuitable for terminal sterilisation. The terminal product is a single-dose prefilled syringe for travel medicine and occupational health administration.

    ParameterAdult monovalentPediatric monovalentCombination A/BMulti-dose vial
    Antigen target1000 U/1.0 mL500 U/0.5 mLPer final combination presentationSame as monovalent
    Al³⁺ content0.5 mg/dose0.25 mg/doseVerified by AAS after poolingSame as monovalent
    Final pH6.8–7.46.8–7.46.9–7.36.8–7.4
    Bulk hold temperature2–8 °C2–8 °C2–8 °C2–8 °C
    Filling methodRotary piston, Type I vialRotary piston, tightened fill limitsDual adsorption trains, low-shear poolingMulti-dose vial, crimp and puncture validation
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    Certification & Compliance
    More Introduction

    The product designated as Hepatitis A Vaccine (Human Diploid Cell), Inactivated — Healive Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a biological active pharmaceutical ingredient consisting of purified, formalin-inactivated hepatitis A virus propagated in human diploid cell culture. The descriptor includes tablet, capsule, granule, injection, oral, and injectable presentations; however, the monographed pharmaceutical form for inactivated hepatitis A virus antigen is the sterile suspension for intramuscular injection. Oral solid dosage forms are not described in Ph. Eur. 1107 Hepatitis A Vaccine (Inactivated, Adsorbed) or in the corresponding USP monograph for Hepatitis A Virus Vaccine Inactivated. No pharmacopoeial standard establishes an oral granule, tablet, or capsule specification for this antigen. The material is therefore handled as a sterile biological drug substance with a parenteral finished dosage form, while the oral presentations listed in the product title require a separate formulation and clinical development pathway that is outside current compendial recognition.

    The Healive product line identifies a manufacturer-specific inactivated hepatitis A vaccine trade designation. The term “Pharma Grade API” in the product title is a distributor descriptor rather than a compendial classification. The active ingredient is non-replicating whole virion antigen, not a recombinant protein or peptide. Because inactivated hepatitis A vaccines from different manufacturers use different reference preparations and unit systems, the label strength of Healive may be expressed in manufacturer-defined antigen units and is not interchangeable with the units used by other products. Unit conversion between trade products is not appropriate for potency comparison; comparative immunogenicity should be based on clinical seroprotection data, not volumetric addition of API.

    Why is the injectable suspension the only compendial dosage form for inactivated hepatitis A antigen?

    Inactivated hepatitis A antigen is a protein-based virion particle with conformational epitopes that are sensitive to acid, protease activity, and thermal stress. The oral route would subject the antigen to gastric acid below pH 3 and duodenal proteases before it could reach gut-associated lymphoid tissue. Without an enteric protective matrix and a mucosal adjuvant, the immune response would be inconsistent and outside the licensed indication. Compendial texts therefore recognize only the injectable suspension. In contrast, the tablet, capsule, and granule designations in the product title may reflect a broad API listing rather than a finished-product license. For tablet or capsule manufacturing, a lyophilized antigen would require cryoprotectants, dry-state stabilization, and rehydration; no monographed acceptance criteria exist for this specific configuration. Published data for oral inactivated hepatitis A antigen in human clinical use is limited.

    Cell substrate and seed qualification follow biological master file protocols. The human diploid cell substrate is expanded as adherent monolayers; master cell bank and working cell bank testing includes identity, karyology, tumorigenicity testing where applicable to new cell lines, and freedom from adventitious agents. The cell culture process uses controlled passage levels to maintain diploid character. Virus harvests are clarified and concentrated by tangential flow filtration, followed by chromatographic purification. Because hepatitis A virus is non-enveloped, solvent-detergent treatment is not a primary inactivation step; inactivation is achieved with dilute formaldehyde under controlled time-temperature conditions.

    Inactivation kinetics, purification trains, and residual clearance constraints

    Formaldehyde inactivation of hepatitis A virus follows a concentration- and temperature-dependent kinetic curve. Critical process parameters include formalin concentration, inactivation temperature, and contact time. License-specific values are not routinely published in open-access documents for Healive; therefore the exact numerical processing window is limited. In general, inactivation is performed to exceed the minimal hold time determined by serial virus passage in susceptible cell cultures, with a safety margin based on inactivation curve studies. After inactivation, residual formaldehyde is removed or reduced by diafiltration, and the release method may follow Ph. Eur. 2.4.18. Host-cell DNA and protein are reduced through ion-exchange chromatography, size-exclusion chromatography, or ultrafiltration, with limits established per ICH Q6B and WHO biological product recommendations.

    The purified antigen is then adsorbed onto aluminum hydroxide or another permitted aluminum salt. Adsorption is not a simple mixing operation. Adsorption efficiency depends on pH, ionic strength, buffer species, and antigen-to-adjuvant ratio. Deviation from the registered pH window can produce incomplete adsorption, free antigen in supernatant, or aggregation; the suspension must remain homogeneous through filling. Because the adsorbed suspension cannot be sterile-filtered after aluminum addition, the antigen bulk is sterile-filtered before adsorption and all downstream operations are conducted aseptically. Sterile filtration of aluminum-containing suspensions is not feasible because the gel phase blocks 0.2 µm membranes.

    On production scale, adherent human diploid cell cultures are expanded in multilayer cell factories, roller bottles, or fixed-bed bioreactors. The choice of equipment influences harvest lot size and cell debris burden. Tangential flow filtration with polyethersulfone cassettes removes cell debris and concentrates the virus harvest; filter fouling and shear-induced aggregation are controlled by transmembrane pressure below a validated limit. Ion-exchange chromatography exploits the virion surface charge, while size-exclusion chromatography separates intact virions from smaller contaminants. These equipment configurations are standard for inactivated viral vaccines; product-specific parameters are licensed and confirmed in process validation batches.

    Compendial release and stability-indicating tests for inactivated hepatitis A vaccine include sterility, bacterial endotoxins, pH, aluminum content, residual formaldehyde, identity, and potency. The following compliance checklist identifies the standard test designations and the manufacturing control point.

    Quality attribute Method or standard designation Control point Technical note
    Sterility USP <71>, Ph. Eur. 2.6.1 Final container after filling Direct inoculation or membrane filtration; incubation typically 14 days at 20–25°C and 30–35°C.
    Bacterial endotoxins USP <85>, Ph. Eur. 2.6.14 Bulk antigen and final container Limit calculated from maximum human dose; parenteral vaccines may use a low limit based on 5 EU/kg or stricter.
    pH USP <791>, Ph. Eur. 2.2.3 Adsorbed suspension Registered range; pH excursions alter aluminum adsorption and suspension uniformity.
    Aluminum content Ph. Eur. 2.5.13 or atomic absorption spectrophotometry Adsorbed bulk Label claim and dose-specific tolerance.
    Residual formaldehyde Ph. Eur. 2.4.18 or equivalent HPLC method Purified antigen before adsorption Residual clearance after diafiltration; monograph-defined limit.
    Identity HAV-specific ELISA with monoclonal antibody panel Bulk antigen Confirmation of hepatitis A virus antigen epitopes.
    Potency Antigen ELISA or immunogenicity assay Released final lots Relative to manufacturer reference standard; not interchangeable across trade products.

    The release list above is a compliance checklist, not a batch-specific certificate. Healive-specific acceptance criteria are defined in the manufacturer’s market authorization dossier and may differ from generic illustrative values. Public pharmacopoeial monographs provide analytical methods rather than product-specific release limits.

    When aluminum-adsorbed HAV antigen enters final fill and cold-chain handling

    Final fill of an adjuvanted biological suspension introduces stricter handling constraints than small-molecule injectables. The sterile antigen bulk is combined with sterile adjuvant under aseptic conditions. After adsorption, the mixture cannot undergo terminal sterilization by steam, gamma radiation, or ethylene oxide without denaturing the antigen and damaging the aluminum gel. The final suspension is therefore filled into sterile containers through low-shear filling systems. Constant agitation with a defined stirrer speed is required to prevent sedimentation in the hold tank; fill weight and volume are monitored by automatic checkweighers and volume verification systems. Container closure integrity testing follows USP <1207>.

    The product must be stored at 2–8°C. Freezing causes aluminum-containing gels to aggregate; the resulting separation can be irreversible and is a critical quality rejection criterion. Temperature excursions above 8°C may reduce antigen stability and shorten shelf life. Time-out-of-refrigeration studies follow ICH Q1A(R2) and ICH Q5C stability guidance. Visual inspection alone is insufficient to assess antigen-adjuvant integrity after thermal stress. A frozen filled syringe must not be used after thawing because freeze-induced aggregation can cause irreversible antigen-adjuvant separation and loss of dose uniformity.

    In contrast to live attenuated hepatitis A vaccines used in some national programs, the Healive inactivated antigen does not contain replication-competent virus. This distinction affects patient selection and cold-chain handling. Inactivated hepatitis A vaccine can be used in immunocompromised travelers when indicated, whereas live attenuated vaccines are generally avoided in that population. Compared with virosomal inactivated hepatitis A vaccine, the aluminum-adsorbed Healive suspension depends on alum depot formation and requires resuspension before administration. The product is monovalent; combination hepatitis A/hepatitis B or hepatitis A/typhoid vaccines require separate antigen compatibility and adjuvant compatibility studies.

    Product category Critical technical difference Manufacturing or clinical consequence
    Healive inactivated versus live attenuated hepatitis A vaccine Non-replicating formalin-inactivated virion; no lyophilized live virus seed Injectable aluminum-adsorbed suspension stored at 2–8°C; different contraindications in immunocompromised populations.
    Healive versus virosomal inactivated hepatitis A vaccine Aluminum salt depot instead of virosomal particle carrier Different syringeability; resuspension required; aluminum content tested at release.
    Healive monovalent versus hepatitis A/HBV or hepatitis A/typhoid combination vaccines Single antigen rather than multiple antigens with combined adjuvants No antigen interference; simpler release panel; fewer combination-specific assays.
    Tablet, capsule, or granule designation versus injectable suspension Protein antigen not enteric-coated or formulated for oral delivery Not compendial for this antigen; oral route would require novel stabilizer, mucosal adjuvant, and clinical bridging data.

    Dilution of the finished suspension in other diluents or mixing with unrelated vaccines in the same syringe is not recommended unless compatibility data are provided in the approved label. The antigen should not be exposed to strong oxidizing agents, cationic detergents at concentrations sufficient to desorb alum, or temperatures above registered limits. If a filled syringe is frozen, it must be discarded after thawing; retention samples cannot substitute for visual inspection of adjuvant integrity. These constraints apply specifically to the injectable presentation. For oral solid or granule development, the bulk antigen would require additional process steps such as lyophilization or spray drying, enteric coating, and dry stabilizer selection. No compendial product-specific acceptance criteria are currently available for oral inactivated hepatitis A antigen, and published data for this specific configuration is limited.

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