| HS Code | 605977 |
| Product Name | Infectious Bursal Disease Vaccine, Inactivated (Strain CJ-801-BKF) Veterinary Grade API |
| Strain | CJ-801-BKF |
| Vaccine Type | Inactivated |
| Pathogen | Infectious Bursal Disease Virus (IBDV) |
| Grade | Veterinary Grade |
| Target Species | Chickens |
| Disease Prevention | Infectious Bursal Disease (Gumboro disease) |
| Physical Form | API suitable for formulation into tablets, injections, capsules, powders, granules, premix, or solutions |
| Adjuvant | Typically formulated with an immunogenic adjuvant for inactivated vaccines |
As an accredited Infectious Bursal Disease Vaccine,Inactivated(Strain CJ-801-BKF) Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged as sterile, sealed veterinary-grade API in moisture-resistant containers. Quantity: 50 g per container. Suitable for tablet, injection, capsule, powder, granule, premix, or solution formulations. |
| Container Loading (20′ FCL) | 20′ FCL loading: temperature-controlled container with palletized, secured drums/cartons of inactivated veterinary vaccine API, using dunnage to prevent shift. |
| Shipping | Ship as hazardous biological material under controlled cold-chain conditions (2–8°C). Use validated insulated containers with gel packs and temperature data loggers. Protect from light, freeze, and breakage. Include veterinary vaccine documentation and comply with international biological shipping regulations. Ensure expedited delivery to maintain API stability and efficacy. |
| Storage | Store at 2–8°C (36–46°F), protected from light and moisture. Do not freeze, as this may damage the inactivated antigen. Keep container tightly closed to preserve potency. Use aseptic handling during preparation. Ensure proper veterinary labelling and keep out of reach of children. Discard unused portions per biohazard waste regulations. |
| Shelf Life | Shelf life: 24 months when stored at 2–8°C, protected from light, in unopened original containers. |
Infectious Bursal Disease Vaccine, Inactivated (Strain CJ-801-BKF) Veterinary Grade API is most frequently formulated into water-in-oil (W/O) emulsion vaccines for subcutaneous or intramuscular administration in breeder pullets. The aqueous phase comprises 30% w/w of the final emulsion and the oil phase 70% w/w. Mineral oil adjuvants of the mannide monooleate type are used; the required hydrophilic-lipophilic balance falls between 4.0 and 6.0. Antigen content is expressed as the pre-inactivation virus titer equivalent per dose; published monographs for inactivated IBD vaccines commonly specify a minimum pre-inactivation titer of 10^5.5 to 10^6.8 CCID50 per dose, although published data for the specific CJ-801-BKF strain configuration is limited. The aqueous phase is prepared in phosphate buffer at pH 7.0–7.4, and the oil phase is sterilized separately by filtration or dry heat. High-shear mixing is performed with an inline Silverson L5T rotor-stator unit at 3,000–6,000 rpm for 3–5 recirculation passes through a 500 L jacketed vessel. Droplet size after emulsification is measured by laser diffraction according to ISO 13320:2020; the acceptance window is Dv50 0.8–1.5 µm and Dv90 ≤ 2.5 µm. If Dv90 exceeds 3.0 µm, the emulsion shows accelerated creaming after 14 days at 37°C. The temperature of the emulsion must not exceed 25°C during mixing because the VP2 neutralizing epitopes are thermolabile and high shear raises bulk temperature at rates of 0.5–1.0°C per pass in uncooled vessels. Sterility of the final emulsion is verified by membrane filtration or direct inoculation according to 21 CFR 610.12. Safety and potency are evaluated by challenge in specified-pathogen-free chickens following OIE Terrestrial Manual 2021, Chapter 3.3.12.
For layer flock priming where injection-site oil residue is unacceptable, an aqueous aluminum hydroxide-adsorbed presentation is used. The final aluminum hydroxide gel concentration is 2.0% v/v; the antigen is adsorbed at 4°C for 16–24 h under gentle stirring at 80–120 rpm. Adsorption is performed in sodium phosphate buffer at pH 7.0–7.4; higher ionic strength competes with antigen binding. The adsorbed formulation has a final viscosity of 5–15 mPa·s at 25°C when measured with a Brookfield LV-3 spindle at 12 rpm according to ASTM D2196-20. The aluminum hydroxide point of zero charge near 11.4 means that negatively charged viral particles adsorb efficiently at neutral pH; however, variation in viral surface charge or lot-to-lot aggregation can reduce adsorption efficiency below 80%. In such cases, the manufacturer may add 0.5–1.0% w/v mannitol as a stabilizer, but published data for this specific configuration is limited. The terminal product is a ready-to-use aqueous suspension for intramuscular injection in layer chickens.
| Parameter | W/O Emulsion | Aluminum Hydroxide Suspension |
|---|---|---|
| Aqueous phase ratio | 30% w/w | 100% aqueous |
| Oil phase ratio | 70% w/w | Not applicable |
| Final viscosity at 25°C | 30–60 mPa·s | 5–15 mPa·s |
| Droplet size acceptance by laser diffraction | Dv50 0.8–1.5 µm; Dv90 ≤ 2.5 µm | Not applicable |
| Standard for droplet size | ISO 13320:2020 | Not applicable |
| Viscosity test method | ASTM D2196-20 | ASTM D2196-20 |
| Administration route | Subcutaneous or intramuscular | Intramuscular |
When the inactivated strain CJ-801-BKF antigen is co-formulated with Newcastle disease virus, infectious bronchitis virus, egg drop syndrome virus, or avian reovirus antigens, the primary process risk is not antigen incompatibility but depletion of the available emulsion interface by additional viral proteins. Each antigen is typically concentrated and buffer-exchanged by tangential flow filtration using a 50 kDa regenerated cellulose cassette to remove incompatible stabilizers and to standardize the aqueous phase at pH 7.2. The total aqueous phase protein content must be measured by Lowry or bicinchoninic acid assay before emulsification; when the protein load exceeds the surfactant capacity of the oil phase, droplet size increases and potency drops. The mixed aqueous phase is added to the oil phase in a 30:70 w/w ratio and emulsified at 3,000–6,000 rpm as in single-antigen emulsions; however, the target Dv50 is relaxed to 1.0–2.0 µm because a larger particle size reduces shear damage to the most thermolabile co-antigen. The final multivalent product is filled into 500 mL high-density polyethylene bottles; each 0.5 mL dose contains the IBDV component at a minimum pre-inactivation titer equivalent determined by lot-to-lot potency testing. Serological monitoring in breeder flocks is used to confirm seroconversion by ELISA at 21–28 days post-vaccination. Batch-to-batch variance is controlled by storing each antigen concentrate separately at -70°C and blending only after potency assay release.
Regional variant pressure may force a manufacturer to bank the CJ-801-BKF antigen at high concentration for later formulation into autogenous or region-specific vaccines. The antigen is concentrated from clarified viral harvest by ultrafiltration using a 100 kDa regenerated cellulose cassette; the retentate is diafiltered against 5–10 volumes of phosphate-buffered saline pH 7.2 to reduce host-cell protein. Before inactivation, live virus titer is determined by CCID50 titration in chicken embryo fibroblasts. Inactivation with formaldehyde at 0.1% v/v at 37°C for 24 h or with beta-propiolactone at 0.05% v/v at 4°C for 16 h is used; published inactivation kinetics for the CJ-801-BKF strain are limited, so each lot is sampled during inactivation and tested for residual live virus by three successive passages in SPF embryonated eggs. Excessive inactivation crosslinks the VP2 neutralizing epitopes and reduces potency; insufficient inactivation fails the safety test described in OIE Terrestrial Manual 2021, Chapter 3.3.12. Residual formaldehyde is measured colorimetrically and must not exceed 0.02% w/v in the final bulk. The inactivated antigen concentrate is stored at -70°C or lyophilized for 36 months stability monitoring. Autogenous vaccine blending typically uses a lower oil-to-aqueous ratio of 50:50 w/w to reduce injection-site reactions in young birds; the final product is released by the same safety and potency tests as licensed vaccines.
| Acceptance parameter | Test method | Typical acceptance criterion |
|---|---|---|
| Freedom from live IBDV | Three blind passages in SPF embryonated eggs (OIE Terrestrial Manual 2021, Chapter 3.3.12) | No mortality, lesions, or viral antigen after passage 3 |
| Sterility | 21 CFR 610.12 membrane filtration or direct inoculation | No growth at 14 days |
| Residual formaldehyde | Colorimetric assay on final bulk | ≤ 0.02% w/v |
| Potency by challenge | Vaccination of SPF chickens followed by virulent IBDV challenge | ≥ 80% protection in vaccinated vs ≤ 20% in controls |
| Emulsion stability | Visual inspection after storage at 37°C for 14 days | No phase separation; Dv90 drift ≤ 0.5 µm |
For long-distance shipment without cold-chain interruption or emergency stockpiling, a freeze-dried powder intermediate is prepared. The inactivated liquid concentrate is formulated with 5% w/v trehalose and 2% w/v mannitol as cryoprotectants, filled into 10 mL Type I glass vials with butyl rubber stoppers, and lyophilized in a stainless-steel tray dryer. The cycle includes freezing at -40°C for 4 h, primary drying at -20°C and 0.2 mbar for 24 h, and secondary drying at 20°C and 0.05 mbar until residual moisture is below 2.0% by Karl Fischer titration according to Ph. Eur. 2.5.12. Rehydrated antigen is not automatically suitable for direct W/O emulsification because lyophilization can induce VP2 aggregate formation; therefore, the reconstituted solution is filtered through a 0.45 µm low-protein-binding PES membrane before oil phase mixing. Published data for freeze-dried inactivated IBDV antigen in the CJ-801-BKF strain configuration is limited, so each lot must be qualified by droplet size stability after reconstitution, not by assuming equivalence to fresh liquid antigen.
Filling line performance is governed by emulsion viscosity drift, not by antigen titer. A W/O emulsion containing 30% aqueous phase and 70% mineral oil typically exhibits viscosity between 30 and 60 mPa·s at 25°C; below 20 mPa·s phase separation occurs in the holding tank, and above 60 mPa·s rotary piston fillers begin to cavitate. The filler is typically a Bausch+Ströbel or Groninger rotary piston machine with 1.0 mm ceramic nozzles; the fill volume is 0.3–0.5 mL per dose. Viscosity is measured inline or at-line every 30 min using a Brookfield viscometer with LV-3 spindle at 12 rpm per ASTM D2196-20. Temperature control at 15–20°C during filling reduces viscosity variation; however, chilling below 10°C can cause mineral oil wax precipitation. Homogenizer heat generated during scale-up from 50 L to 500 L batches shifts droplet size distribution toward larger Dv90, which can increase viscosity non-linearly. Therefore, the emulsion is cooled through a plate heat exchanger immediately after the final homogenizer pass with an outlet temperature setpoint of 18°C.
In the target poultry species, tablets, capsules, powders, granules, and premix formats are not recognized industrial delivery forms for inactivated IBDV antigen. The inactivated whole virus particle is acid-labile and is degraded in the avian proventriculus and gizzard before it reaches the ileal lymphoid tissue; therefore, oral administration of uncoated antigen does not induce a primary immune response. Published data for controlled oral delivery of inactivated IBDV antigen in chickens is limited, and no registered product in this configuration is known. If a manufacturer attempts a dry oral premix, the antigen must be spray-coated with an enteric polymer such as Eudragit L100-55 at a coating level of 10–20% w/w relative to the granule mass, but the batch-to-batch variability in gastric emptying, gizzard retention time, and intestinal pH makes reproducible antigen presentation unlikely. The powder or granular API form is therefore reserved for downstream vaccine formulation intermediates, such as lyophilized antigen banks, rather than for direct oral administration. Capsule and tablet formats are not appropriate for mass poultry administration.
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The full product designation, Infectious Bursal Disease Vaccine, Inactivated (Strain CJ-801-BKF) Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions, identifies an inactivated whole-virus infectious bursal disease virus antigen concentrate intended solely as a starting material for veterinary finished-product manufacturing. The designation does not indicate that the API is ready for direct administration in all listed presentations; rather, it defines the range of finished dosage forms into which the antigen may be formulated after downstream processing. The inactivated antigen does not replicate in recipient birds, so the safety risk profile associated with live attenuated IBDV strains—vaccine-induced bursal follicle depletion, immunosuppression, and reversion to virulence—does not apply to the concentrated antigen itself. The primary route of finished-product administration remains injection; oral solid and premix presentations require separate formulation development and species-specific challenge data.
The API is expected to be released with a certificate of analysis covering sterility, inactivation, potency, residual moisture, pH, and identity. Release methods are generally aligned with Ph. Eur. 0588 for inactivated avian infectious bursal disease vaccine and 9 CFR 113.206 for avian infectious bursal disease vaccines, depending on the target regulatory jurisdiction. Because the product is a veterinary-grade API, not a fully formulated vaccine, the finished dosage form manufacturer is responsible for final potency claims, adjuvant compatibility, target species safety, and stability under the proposed label. The API supplier should also provide master seed lot documentation and passage-level data for the CJ-801-BKF strain, because the strain designation alone does not define its immunogenicity or its phylogenetic relationship to circulating IBDV field variants.
Liquid presentations are typically held at 2–8 °C and protected from repeated freeze-thaw cycles. Lyophilized presentations are usually prepared with carbohydrate or amino acid cryoprotectants to reduce ice-crystal damage to the viral capsid; residual moisture in the lyophilized cake is commonly controlled to ≤ 2.0% w/w by Karl Fischer titration, and headspace residual oxygen should be monitored when vials are sealed under vacuum or inert gas. For powdered intermediates intended for tableting or premix blending, the antigen may be adsorbed onto carriers such as lactose, dextrin, mannitol, or calcium carbonate; dry blend uniformity should be verified by assay of the active fraction, and segregation tendencies should be assessed across a particle-size range that avoids excess dust below 100 µm and oversized granules above 1 mm.
Production-scale concentration of inactivated IBDV antigen is usually performed by tangential-flow ultrafiltration with a molecular weight cut-off of 100–300 kDa; transmembrane pressure is maintained below 1.0 bar to limit antigen aggregation. The concentrated retentate may be diafiltered against buffer at 2–8 °C to remove low-molecular-weight media components and free inactivation by-products. This step must be monitored by antigen capture ELISA, because membrane polarization can reduce flux and increase local antigen concentration, promoting aggregate formation that may reduce final potency.
Inactivation of the CJ-801-BKF antigen is validated using an alkylating agent or another approved inactivant; the selection and residual level are batch-specific and must be stated on the certificate of analysis. Residual infectivity is assessed by blind passage in embryonated chicken eggs or susceptible cell cultures, and acceptance is based on absence of live virus after at least three consecutive passages. In vivo confirmation may include absence of bursal lesions in inoculated birds at 21 days post-inoculation. Sterility testing is performed according to Ph. Eur. 2.6.1 or 9 CFR 113.26; the method is selected by the physical state of the bulk antigen, with membrane filtration or direct inoculation used for viscous concentrates. Endotoxin and mycoplasma control are supplier-dependent but should be included in the master seed and production culture program.
Potency is commonly expressed as relative potency by ELISA or virus neutralization against a reference serum panel. The release limit for the API is not fixed in international compendia and must be justified by the finished-product manufacturer; a typical acceptance criterion is not less than 1.0 relative potency unit when the concentrated antigen is formulated into the target injectable vaccine. Residual moisture in lyophilized API is controlled to ≤ 2.0% w/w. pH of aqueous concentrates is usually held between 7.0 and 7.6, but the exact range depends on buffer composition and subsequent emulsion conditions. In-process controls should also verify that the inactivation step has not hydrolyzed VP2 epitopes, since excessive inactivation time or temperature can reduce ELISA reactivity and final neutralizing antibody responses. SDS-PAGE and Western blot profiles against VP2-specific monoclonal antibodies are therefore used to compare pre- and post-inactivation antigen integrity.
| Parameter | Typical control criterion | Reference method |
|---|---|---|
| Sterility | No growth in thioglycollate and soybean-casein digest media | Ph. Eur. 2.6.1 / 9 CFR 113.26 |
| Inactivation | No live IBDV after three passages in embryonated chicken eggs | Ph. Eur. 0588 / 9 CFR 113.206 |
| Residual moisture (lyophilized) | ≤ 2.0% w/w | Karl Fischer titration |
| Potency | Not less than 1.0 relative potency unit | ELISA / challenge |
| Storage | 2–8 °C, protect from light | Manufacturer stability program |
The central constraint is conformational stability of the inactivated viral particle during drying, compression, and gastrointestinal transit. Lyophilization can preserve antigenicity when the antigen is embedded in a glassy matrix, but tablet compression imposes additional mechanical stress; compression pressures above 80 MPa are generally incompatible with uncoated viral antigen preparations unless protective excipients such as trehalose, polyvinylpyrrolidone, or enteric polymers are used. Even when tablet integrity is acceptable, dissolution in the avian gastrointestinal tract exposes the antigen to acidic pH below 3.0 and proteolytic enzymes, which can degrade surface epitopes. Published data for this specific configuration is limited; therefore, tablets and capsules should not be assumed to be bioequivalent to injectable emulsion vaccines without controlled challenge studies.
For granules and premixes, the processing sequence affects antigen recovery. Spray-drying or fluid-bed granulation at inlet temperatures above 60 °C may cause antigen aggregation, and the carrier material can alter rewetting and dispersion in drinking water or feed. If a dry premix is intended for oral administration, the formulation must demonstrate antigen survival under the pH, enzymatic, and transit-time conditions of the target species. The use of enteric-coated granules, liposomal dispersions, or pH-sensitive matrices can provide delayed release, but each added coating step reduces yield and requires dissolution testing. For aqueous solutions, stability is highest in buffered media at 2–8 °C; unpreserved reconstituted solutions should generally be used within 4 hours unless the manufacturer’s stability studies support longer hold times.
| Dosage form | Typical processing route | Principal technical constraint |
|---|---|---|
| Injectable emulsion | High-shear emulsification | Droplet size distribution, shear-induced heat |
| Tablet | Lyophilization, blending, compression | Compression pressure, residual moisture |
| Capsule | Dry granulate filling | Gastrointestinal degradation, antigen release |
| Powder / granule / premix | Adsorption, spray drying | Carrier segregation, heat exposure |
| Solution | Buffered aseptic preparation | Hydrolysis, aggregation, cold-chain stability |
Injectable formulations based on CJ-801-BKF inactivated antigen typically use a water-in-oil or water-in-oil-in-water adjuvant matrix. The aqueous antigen phase is combined with an emulsifier such as mannide oleate and a mineral or metabolizable oil, with the aqueous phase commonly representing 30–50% of the total volume. High-shear rotor-stator mixing at 3,000–10,000 rpm is used for small- to pilot-scale batches, but production-scale equipment requires cooling jackets or intermittent mixing because shear-induced temperature rise can push the bulk antigen above 20 °C, increasing the risk of antigen denaturation. The resulting droplet size distribution is measured by laser diffraction; a volume-mean diameter that is too small may delay antigen release, whereas droplets that are too large can cause injection-site reactions and emulsion instability.
For breeder chickens, the final injectable dose is commonly 0.5 mL administered intramuscularly or subcutaneously after primer administration with a live or immune-complex vaccine, but the exact dose and timing are determined by the finished-product marketing authorization. The emulsion should be stored at 2–8 °C and should not be frozen; freeze-thaw cycles can crack the emulsion and release free antigen, altering potency and initiating instability. Syringeability and resistance to sedimentation are controlled by viscosity measurements, usually at a defined shear rate and temperature such as 25 °C. Incompatibilities include direct mixing with aqueous diluents without proper emulsification, because the vaccine may separate into oil and water phases and deliver an unpredictable antigen dose. Strong oxidizing agents, extremes of pH below 5.0 or above 8.5, and cationic surfactants that displace antigen from emulsion interfaces should also be avoided during formulation.
In relation to other IBD vaccine technologies, the inactivated whole-virus CJ-801-BKF API differs from live attenuated products in that it cannot replicate, cannot revert to virulence, and does not cause vaccine-induced bursal atrophy; however it also does not provide rapid mucosal immunity and therefore is not suitable as a single-dose primary vaccine in most production programs. Compared with VP2 subunit or virus-like particle constructs, the inactivated whole-virus preparation retains additional viral structural proteins, which may broaden antibody responses but can complicate serological differentiation between vaccination and field infection. Compared with recombinant HVT-IBD vector vaccines, the CJ-801-BKF API does not introduce a herpesvirus vector backbone into the recipient and is not administered in ovo by the API supplier; onset of protection is slower and depends on adjuvanted depot formation. Compared with immune-complex vaccines, the CJ-801-BKF antigen does not contain infectious virus and can be shipped as a non-infectious liquid or lyophilized solid. The principal operational boundary is that oral tablets, capsules, powders, granules, and premixes containing inactivated IBDV antigen are not standard reference presentations, and their development should be treated as experimental unless supported by published species-specific challenge data or regulatory approval.