| HS Code | 679049 |
| Product Name | Yujin Oral Solution Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Product Type | Veterinary Grade Active Pharmaceutical Ingredient (API) |
| Grade | Veterinary Grade |
| Primary Form | Oral Solution |
| Compatible Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Intended Use | Manufacturing of veterinary pharmaceutical dosage forms |
| Target Species | Veterinary animals |
| Route Of Administration | Oral or as determined by final dosage form |
| Manufacturer | Yujin |
| Regulatory Status | Veterinary use only |
As an accredited Yujin Oral Solution 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 | Packaging: 25 kg double-lined fiber drums containing Yujin Oral Solution Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions. |
| Container Loading (20′ FCL) | A 20′ FCL container loading: Yujin Oral Solution Veterinary Grade API securely packaged, labeled, and properly sealed for export shipment. |
| Shipping | Yujin Oral Solution Veterinary Grade API—tablets, injections, capsules, powders, granules, premix, or solutions—is shipped in sealed, UN-approved containers labeled per IATA/ADR/IMDG rules. Depending on stability, ambient or temperature-controlled transport is used. Shipments include SDS, COA, packing list, and customs documentation. Handle as a regulated veterinary chemical. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature (15–25°C), unless the label or certificate of analysis specifies otherwise. Keep containers tightly closed, protected from light, moisture, and contamination. Segregate from food, feed, and incompatible chemicals. Use appropriate PPE, follow local regulations and the safety data sheet, and keep away from children and animals. |
| Shelf Life | Shelf life varies by dosage form; typically 24–36 months if stored sealed, cool, dry, and protected from light, per manufacturer. |
The Yujin Oral Solution veterinary-grade API is released for aqueous bulk manufacturing in group medication programs for swine and poultry. Stock solutions are prepared at 10.0–20.0% w/v active concentration in 5,000 L 316L stainless steel mixing vessels, then diluted through drinking water proportioners to final administration levels between 10 mg/L and 100 mg/L depending species mass, daily water intake, and therapeutic indication. The batch process includes heating deionized water to 30±2°C, adding the API under high-shear dispersion at 900–1,200 rpm, and adjusting pH into the 4.5–5.5 range with citrate buffer before recirculation through a 0.45 µm cartridge filter for 20 min. Release testing against EU 2019/6 Annex II quality requirements, 21 CFR 514.1(b)(4), and VICH GL3 stability protocols includes active assay by HPLC, pH, density, clarity, and sedimentation after 24 h at 25°C. Production-scale failure modes include pH drift above 0.3 units after 72 h in high-bicarbonate farm water and visible precipitation when raw water hardness exceeds 250 mg/L CaCO₃; both conditions require pre-treatment or citrate-buffered dilution before batch release. Terminal product forms in this stream are single-species oral drench solutions, drinking water concentrates, and proportioner-ready stock solutions.
Parenteral administration imposes two independent release barriers: sterility and pyrogen load. The injectable line is compounded at active concentrations bracketed between 20.0 mg/mL and 50.0 mg/mL, equivalent to 2.0–5.0% w/v, with osmolality adjusted to 280–320 mOsm/kg using sodium chloride. Terminal moist heat sterilization is used where thermal stability data permit: filled Type I glass vials are autoclaved at 121°C for 15 min, with validated F0 not less than 8 min for the 10 mL and 50 mL load patterns. Where the active substance is heat-sensitive, sterile filtration through two 0.22 µm polyethersulfone membrane filters is completed immediately before aseptic filling in an ISO 7 cleanroom; filter integrity testing is performed before and after each batch by diffusion flow or water intrusion. Endotoxin release limits comply with Ph. Eur. 5.1.1, USP <85>, and VICH GL3, with intramuscular and subcutaneous formulations tested against route-specific pyrogen budgets. A documented processing bottleneck occurs when membrane loading is allowed to exceed 250 g/m²; transmembrane pressure rises rapidly and filter capacity becomes non-linear, forcing split filtration and increasing the sterility risk surface. Finished injectable products include ready-to-use solutions and, for thermolabile batches, lyophilized powder for reconstitution in veterinary parenteral packaging.
Tablet compression of the veterinary API is defined less by dissolution behaviour than by particle-size distribution, flowability, and compressibility. The API is screened through a 0.5 mm cone mill and combined with microcrystalline cellulose and lactose monohydrate at active loadings of 2.0–8.0% w/w for direct compression. Above 8.0% w/w, roller compaction is introduced to preserve powder flow and reduce segregation during long blenders runs. Blend uniformity follows Ph. Eur. 2.9.40 and USP <905>; tablets are released against friability below 1.0% under Ph. Eur. 2.9.7 and disintegration below 15 min under USP <701> for immediate-release claims. On a 16-station rotary press, typical compression force is 12–18 kN at 20–40 rpm, with ejection force monitored because magnesium stearate above 1.5% w/w is an operational incompatibility that induces capping and lamination. If wet granulation is required for taste-masking or higher loading, purified water binder solution is used and fluid-bed drying is set to inlet air 50–60°C with final granule moisture limited to 1.5–3.0% w/w. Terminal products in this downstream segment are uncoated oral tablets, film-coated tablets, and chewable tablets for companion animals.
Low-dose capsule filling demands a validated combination of gravimetric fill control and blend homogeneity because active loading may fall to 0.5–2.0% w/w for small companion-animal dose units. The API is wet-granulated with povidone K30 at 3.0% w/w binder, dried in a fluid-bed dryer to residual moisture 1.0–2.5% w/w, milled, and filled into size 3 hard capsules. Capsule content uniformity release follows Ph. Eur. 2.9.40 and USP <905>, while dissolution analysis is conducted with USP Apparatus II at 50 rpm in 900 mL of pH 6.8 phosphate buffer. The production line uses an automatic capsule loader operating at 25,000–60,000 capsules/h; fill mass is checked at intervals not exceeding 30 min to detect drift caused by powder density shifts. A 1:5 premix of API with lactose monohydrate is standard before main blending to control batch-to-batch variance and prevent low-dose content deviation. Granulation increases bulk density and reduces dust, but over-drying below 1.0% w/w moisture creates electrostatic adhesion inside the dosator, causing fill variation. Finished capsule types include hard gelatin capsules and hydroxypropyl methylcellulose capsules for cats and dogs.
For water-soluble oral powders, a separate production line addresses commercial shipments where bulk liquid transport is uneconomical. The API is dry-blended with glucose or lactose at active loadings of 1.0–10.0% w/w, then granulated in a top-spray fluid-bed granulator using purified water as binding liquid. Inlet air is set at 55±5°C, outlet air at 28–34°C, and atomizing air pressure at 1.5–2.5 bar; granule sizing follows through a 1.0 mm screen with final moisture controlled at 1.0–2.0% w/w. A production-scale defect is oversized agglomerate formation when spray rate exceeds 35 g/min per nozzle, reducing dissolution speed in cold water and altering proportioner flow characteristics. Compliance for this segment is drawn from EU 2019/6 Annex II and 21 CFR 514.1; release testing includes solubility of 100 g product in 1 L water at 20°C with no visible residue after 5 min and concentration variation not exceeding ±5% over 24 h at 25°C. Terminal products are water-soluble sachet powder, granulated oral powder packaged in aluminium-lined sachets, and bulk granulated material for drinking water proportioners.
Medicated premix manufacturing requires a segregated line because cross-contamination control is a GMP obligation under 21 CFR 225.1 for medicated feed and EU Regulation 2019/4. Stock premix is manufactured at an active concentration of 5.0–20.0% w/w, then diluted through the feed mill to final feed concentrations between 0.01% w/w and 0.1% w/w depending species, body weight, and daily feed intake. A ribbon mixer with 1,000 kg working capacity is used for final blending; the API is first premixed with wheat middlings or calcium carbonate at a 1:9 ratio to reduce electrostatic segregation. Mixing time is established by homogeneity sampling, typically 10–15 min at 12 rpm, with release criteria requiring assay CV below 5% across 10 sampling points. Batch cleanout uses 50 kg wheat middlings as flushing material, and carryover limits are verified by assay after flush completion. The main processing variable is relative humidity: at levels below 30%, static adhesion to ribbon mixer walls increases and reduces final assay recovery, requiring controlled humidification of the processing room. Terminal products in this stream are granulated in-feed premix, meal premix, and pelleted medicated feed for swine, poultry, and ruminant species.
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The Yujin Oral Solution Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a liquid active pharmaceutical ingredient supplied for incorporation into multiple veterinary dosage forms. The designation identifies a single liquid grade rather than a finished oral solution; it is intended for further pharmaceutical processing under current good manufacturing practice. In the current technical dossier, no additional numeric model code is assigned beyond the full descriptive name. The grade is released against specification classes covering identity, assay, related substances, residual solvents, elemental impurities, endotoxins, bioburden, viscosity, density, clarity, and pH. In downstream use, the liquid form eliminates dry-milling and particle-size control steps that constrain solid API grades, while placing greater emphasis on solvent residue, chemical stability in solution, and low-endotoxin handling for injectable applications. Manufacturing operations using the product are subject to EU 2019/6 and FDA 21 CFR Part 210/211 where the resulting veterinary medicinal product is registered in the relevant jurisdiction.
Release testing follows pharmacopoeial and dossier-defined methods. The table below lists representative specification classes; lot-specific values are recorded on the certificate of analysis and may differ according to the registered market. Where a pharmacopoeial monograph applies, assay is commonly controlled from 95.0% to 105.0% of label claim for oral liquid presentations, although internal release limits may be narrower. Because the product is a liquid, particle-size distribution and powder flow are not release attributes. Instead, density and viscosity become critical because they determine dispensing accuracy and line transfer behaviour.
| Attribute | Test method or standard | Control objective |
|---|---|---|
| Appearance, clarity, and colour | Visual inspection; Ph. Eur. 2.2.1; Ph. Eur. 2.2.2 | Absence of visible particulates and unacceptable opalescence before dilution |
| Assay | HPLC with pharmacopoeial reference standard; Ph. Eur. 2.2.29 | Declaration of active content per millilitre for batch-charging calculations |
| Related substances | HPLC; Ph. Eur. 2.2.29 | Limits according to registered monograph or dossier; individual and total related substances |
| Residual solvents | Headspace GC; VICH GL18; ICH Q3C | Class 1 solvents absent; Class 2 solvents within permitted daily exposure limits |
| Elemental impurities | ICP-MS or ICP-OES; ICH Q3D | Risk-based control according to route of administration and maximum daily dose |
| Bacterial endotoxins | LAL test; Ph. Eur. 2.6.14 | Derived from finished product limit and maximum veterinary dose per kilogram |
| Bioburden | Membrane filtration; Ph. Eur. 2.6.12 | Controlled to support terminal or aseptic processing; non-sterile oral forms commonly meet Ph. Eur. 5.1.4 acceptance criteria |
| Viscosity | Rotational viscometer; Ph. Eur. 2.2.10 | Pumpability, sprayability, and filtration time across manufacturing sites |
| Density | Oscillating density meter; Ph. Eur. 2.2.5 | Conversion from volume to mass for weigh-batch and continuous metering systems |
| pH | Potentiometry; Ph. Eur. 2.2.3 | Stability and compatibility with acid-sensitive or base-sensitive excipients |
On production-scale liquid API receiving lines, viscosity and density are measured at 20 °C before tank transfer. Positive-displacement diaphragm pumps and magnetically coupled gear pumps are commonly used for metering. Lot-to-lot viscosity variation outside the release band has been observed to shift mass-flow calibration by more than the 2% balance tolerance used in solid dosage form dosing. For this reason, the liquid grade is not treated as a fixed-volume commodity; density-corrected weight measurements are specified for batch charging. Where automated addition is used, load-cell-based mass-flow verification provides better traceability than volumetric counters alone.
Storage of the liquid API requires protection from light and freezing. If a frozen or near-frozen condition occurs, phase separation or precipitation may be irreversible, and the product should be rejected unless a thawing and re-qualification procedure has been validated for the specific container type and fill volume. Published data for this specific configuration is limited, so regional stability data and the marketing authorisation dossier remain the controlling documents.
Solid veterinary API grades are typically controlled by particle-size distribution, specific surface area, bulk density, flowability, and sometimes electrostatic charge. Those attributes affect blend uniformity, die filling, roller compaction, and dry granulation. Replacing a solid grade with the oral solution grade removes particle-size distribution as a release attribute and reduces dust exposure during charging. The active is already in solution, so content uniformity challenges in powders and granules shift from mechanical distribution of solid particles to uniform liquid dispersion and drying.
This does not make the liquid grade universally interchangeable. Solution-state chemical stability is the limiting factor. Hydrolytic degradation, oxidation, or microbial growth can occur if the API is held in inadequately sealed containers or exposed to excessive headspace oxygen. The specification therefore includes related substances and bioburden controls intended to detect deterioration before release. In addition, residual solvents are more prominent in a liquid grade than in a dried solid API because the vehicle remains in the product. Downstream users must evaluate whether the stated residual solvent profile is acceptable for the target species and withdrawal period.
A further distinction from solid APIs is the absence of dry-milling heat and shear. Thermally labile actives that degrade during micronization may be handled more safely in solution, provided the solvent system does not introduce a comparable degradation pathway. Conversely, actives that are poorly stable in aqueous or hydroalcoholic vehicles are less suited to this grade. The manufacturer’s dossier limits the permissible dilution matrices and should be consulted before blending with propylene glycol, glycerol formal, benzyl alcohol, or polyethylene glycol grades intended for parenteral use.
The liquid API is introduced at different points depending on the target dosage form. The table below summarises the incorporation point, critical processing parameter, and common equipment class for each format.
| Dosage form | Incorporation point | Critical processing parameter | Representative equipment |
|---|---|---|---|
| Oral solution | Direct dilution in mixing vessel | Final pH, clarity, preservative compatibility, dose accuracy | Jacketed stainless steel vessel with bottom-entering agitator |
| Tablets | Wet-granulation binder solution | Spray rate, granule moisture, drying temperature, tablet hardness | High-shear granulator, twin-screw granulator, fluid-bed dryer |
| Capsules | Granulated powder fill or liquid-filled hard capsule | Granule moisture content, flowability, assay uniformity, capsule brittleness | Planetary mixer, capsule filling machine, sealing station |
| Injections | Dilution with Water for Injection, aseptic filtration | Endotoxin, bioburden, filter compatibility, final sterilisation risk | Stainless steel aseptic filling line, 0.22 μm membrane filter |
| Powders and granules | Adsorption onto carrier | Liquid loading, blend uniformity, residual solvent, flow after adsorption | Ribbon mixer, fluid-bed dryer, conical screw mixer |
| Premix | Spray onto feed carrier | Distribution, segregation during transport, stability on feed matrix | Low-shear mixer, vertical screw conveyor |
Tablet and capsule batches made with the oral solution grade typically introduce the liquid at the wet-granulation stage. A binder solution containing the API is sprayed through a two-fluid nozzle into a high-shear granulator; impeller tip speed and spray rate are adjusted to avoid overwetting. Overwetting produces oversized agglomerates that dry with hard shells and moist cores, causing tablet capping and variable dissolution. Underwetting produces weak granules and poor tablet crushing strength. The same liquid feed can be used in continuous twin-screw granulation, where barrel fill ratio and screw configuration determine granule size distribution more strongly than the API viscosity alone.
For powders and granules, the liquid is adsorbed onto a low-moisture carrier such as microcrystalline cellulose, precipitated silica, or a feed-compatible carrier. Adsorption capacity must be verified by rheological and flow measurements; liquid loading beyond the experimentally determined capacity produces a wet mass that blocks rotary tablet press feed frames or forms non-uniform granules. Residual moisture after drying is controlled by loss on drying and may influence chemical stability, capsule shell integrity, and premix microbial growth.
For veterinary premixes, the liquid grade is sprayed onto a feed carrier under low-shear ribbon blending. The main process risk is segregation after discharge because the API resides on the carrier surface rather than inside a granule. Bulk transport and auger transfer can generate fines that differ in active content from the parent blend. Accordingly, blend uniformity testing and subsequent in-process sampling are required to demonstrate that the active remains distributed after transfer and filling into sacks or bins.
Parenteral processing with the same API requires additional controls. The oral solution grade is not supplied as sterile; therefore downstream sterile filtration or terminal sterilisation is required. The maximum endotoxin level is derived from the finished product specification and the highest veterinary dose per kilogram: the formula K/M is applied, where K is the threshold pyrogenic dose and M is the maximum bolus dose in mg/kg. For a finished parenteral system with a Ph. Eur. 2.6.14 LAL limit of 0.5 EU/mL, the API contribution must be assigned so that the sum of API, excipient, and container closure contributions remains below that limit. Published data for this specific configuration is limited, so each manufacturing site must perform a filter compatibility study using the actual liquid grade and its intended dilution ratio.
Filtration scale-up should include a pre-filtration optimisation trial. Diluted solutions may require a 0.45 μm prefilter before the sterilising 0.22 μm membrane if insoluble excipient fractions or visible particulates appear during mixing. Polyethersulfone and polyvinylidene fluoride membranes are commonly screened; membranes with poor chemical compatibility can exhibit premature fouling or extractable shift. The product should not be assumed autoclavable without temperature-stability data. The current dossier does not provide universal terminal sterilisation parameters, so the final dosage form must be validated for the specific container type, fill volume, and autoclave load pattern.