| HS Code | 144060 |
| Product Name | Jianji Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Product Type | Veterinary Active Pharmaceutical Ingredient |
| Grade | Veterinary Grade |
| Physical Form | Powder |
| Dosage Form Compatibility | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Application | Active pharmaceutical ingredient for veterinary formulations |
| Target Species | Veterinary animals |
| Quality Standard | Veterinary grade |
| Customization | Available for listed dosage forms |
As an accredited Jianji Powder 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 in 25 kg sealed fiber drums with double polyethylene liners, suitable for Jianji Powder Veterinary Grade API. |
| Container Loading (20′ FCL) | 20′ FCL container loading for Jianji Powder Veterinary Grade API, suitable for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Jianji Powder Veterinary Grade API is shipped in sealed, moisture-proof, light-resistant containers with batch, grade, and handling labels. It is transported in cool, dry, ventilated conditions, away from food, feed, and incompatible substances. Shipping includes COA, MSDS, and regulatory documentation; avoid moisture, direct sunlight, and contamination during air, sea, or courier transit. |
| Storage | Store Jianji Powder Veterinary Grade API in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and incompatible substances. Store only in original or approved containers. Keep containers tightly closed and clearly labeled. Maintain segregation from food, feed, and other chemicals. Use clean, dedicated equipment to prevent cross-contamination. Follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Typically 24 months from manufacture when kept sealed, cool, dry, and protected from light; confirm exact expiry with manufacturer. |
In commercial swine production, the medicated feed premix is the most direct route for Jianji Powder Veterinary Grade API when oral ingestion over a fixed 7–14-day course is required. The API is blended with a calcium carbonate carrier having a particle size distribution not exceeding 150 µm at a nominal inclusion of 1.0–2.5 wt% in the intermediate premix, corresponding to 200–500 g per metric tonne of complete feed after dilution at the feed mill. The dry-blending operation runs in a single-shaft ribbon mixer with working volume held at 60–70% of rated capacity for 12–18 minutes at 20–25 rpm; batch records from production-scale mixers of 500–1,000 L indicate that loading the API between two thirds of the carrier volume and the remaining carrier reduces dead-zone residue and keeps the coefficient of variation below 5% as measured by ISO 6497:2020 sampling of ferrous tracer. Moisture in the incoming API above 8% is the primary cause of bridging at the rotary screw feeder; pre-drying in a forced-air oven at 40–45 °C for 2–3 hours is required at relative humidity greater than 60%. The homogenized blend is packed as 5% or 10% medicated premix into 25 kg polyethylene-lined paper sacks compliant with Commission Regulation (EU) 2019/4 Annex II for composition and cross-contamination control, with residue carryover limits referenced in Regulation (EC) No 183/2005 for feed hygiene. Because the API contains hygroscopic polysaccharide fractions, the sacked premix should not be stored directly on concrete floors longer than 72 hours; pallet retention of the sealed sack with desiccant sachets maintains a moisture content of 3.5–4.5% and avoids caking.
When a parenteral route is selected for large animals, Jianji Powder Veterinary Grade API is dissolved in Water for Injection at a concentration of 2.0–4.0 wt% of total extract solids, with 0.9% w/v benzyl alcohol added for multi-dose vials. The pH must be held within 5.5–6.8; above pH 7.0 the tannin–protein complexes precipitate as visible floc and block the 0.22 µm membrane filter during aseptic filling. A 5-micron pre-filter followed by dual 0.22 µm PVDF filters in series is standard practice. Viscosity at 25 °C should remain below 10 mPa·s before filtration; if exceeding this threshold, dilution by an additional 0.3–0.5 volume of WFI is performed rather than increasing pump pressure. Terminal autoclaving at 121 °C for 15 minutes may darken the solution and reduce pH, so sterile filtration followed by aseptic filling is preferred. The filled solution is sealed in 20 mL amber ampoules for single-dose use or 50 mL multi-dose vials with halogenated rubber stoppers. Sterility conforms to Ph. Eur. 2.6.1 and endotoxin is controlled to less than 0.2 EU/mg by Ph. Eur. 2.9.22; particulate matter is validated by Ph. Eur. 2.9.19 for visible and sub-visible particles. Process data from isolator-based filling lines show that the critical hold time between bulk solution preparation and completion of filling should not exceed 8 hours at 10–15 °C to limit microbial bioburden and oxidative degradation of polyphenol fractions. Multi-dose vials require preservative efficacy testing per Ph. Eur. 5.1.3.
Before an in-line medicator delivers a course of treatment to broilers, the water-soluble powder must remain completely dispersible at 5–10 °C, because the drinking water temperature in winter sheds falls into that range. The finished oral powder is prepared by wet granulation in a high-shear mixer with 3–5% w/w of a maltodextrin binder solution, then dried in a fluid-bed dryer at inlet air 60±5 °C, exhaust 38–42 °C, to final moisture ≤4.0%; the dried granules are passed through a 100–212 µm sieve. The API inclusion in the finished water-soluble powder is 15–30 wt%, resulting in an administration rate of 0.25–0.75 g API equivalent per litre of drinking water when a stock solution at 1:50 dilution is metered by a proportional injector. Dispersion time at 10 °C in 150 ppm hardness water is checked against a 30-minute half-life of the suspended matter; if undissolved particles settle faster than that, the batch is reprocessed with an additional 1.0% sodium bicarbonate as a wetting and pH-stabilizing carrier. Compliance for the dosage form sits under EU GMP Part II for veterinary oral soluble powders and the general monograph for granules and powders for oral solutions referenced in Ph. Eur. 2.9.12 for particle size distribution. The terminal packaging is 100 g and 500 g laminated foil sachets with a desiccant window, and the labelled content is verified by HPLC for marker polysaccharide hydrolysate rather than by UV absorbance alone.
| Dosage system | API inclusion ratio | Critical process control | Finishing specification |
|---|---|---|---|
| Swine medicated premix | 1.0–2.5 wt% in intermediate premix; 200–500 g/t complete feed | Ribbon mixer 60–70% fill volume; 12–18 min at 20–25 rpm; CV ≤5% | Moisture 3.5–4.5%; 25 kg sack |
| Injectable solution | 2.0–4.0 wt% of extract solids | pH 5.5–6.8; viscosity ≤10 mPa·s at 25 °C; dual 0.22 µm filtration | Sterility Ph. Eur. 2.6.1; endotoxin ≤0.2 EU/mg |
| Poultry water-soluble powder | 15–30 wt% in powder; 0.25–0.75 g/L drinking water | Fluid-bed inlet 60±5 °C; exhaust 38–42 °C; granule 100–212 µm | Moisture ≤4.0%; dispersion stable 30 min |
| Companion-animal tablet | 120–200 mg per 500 mg tablet; 24–40 wt% of mass | Compression force 20–25 kN; pre-compression 4–6 kN; speed 60–80 rpm | Friability ≤0.8% by USP 1216; disintegration ≤30 min |
| Ruminant oral drench | 5.0–8.0 wt% in propylene glycol base | High-shear mixing 1,500–2,000 rpm for 25–30 min; temperature ≤45 °C | TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g |
| Equine feed top-dress granules | 15–25 wt% in granules; 10–20 g per 500 kg body weight | Fluid-bed inlet 35–40 °C for 45–60 min; granule 500–1,180 µm | Moisture 3.0–4.2%; fines ≤10% |
Direct compaction of the powder into tablet form requires substitution of the API’s natural high hygroscopicity with a microcrystalline cellulose-based direct compression matrix. Each 500 mg scored tablet contains 120–200 mg of API, corresponding to 24–40 wt% of tablet mass; the remaining mass is formed by microcrystalline cellulose at a 50/50 blend of PH-101 and PH-102, 3.0 wt% croscarmellose sodium, 1.5 wt% colloidal silicon dioxide, and 1.0 wt% magnesium stearate. The blend is mixed in a 200 L V-blender for 15 minutes at 15 rpm, with the lubricant added in the final 3 minutes to avoid shear-induced hydrophobic film formation. Compression is carried out on a 16-station rotary tablet press at 20–25 kN, dwell time 20–35 ms, and turret speed 60–80 rpm; pre-compression force is set at 4–6 kN to release air from the high-fiber material. Tablets must remain below 0.8% friability by USP 1216 and disintegrate within 30 minutes in 900 mL water at 37±2 °C per USP 701. At relative humidity above 50%, the powder picks up moisture rapidly and causes picking on the upper punch; feeding room RH must be maintained at 35–45% and the granulation bowl is used only for a 30-minute homogenization of the dry blend if the sieve fraction below 74 µm exceeds 60%. Terminal product is a 30-, 60-, or 90-count HDPE bottle with a desiccant canister and induction-sealed liner, labelled for companion-animal oral administration.
For transition dairy cows, the need for a rapidly absorbed oral solution differs sharply from a dry top-dress because first-pass rumen degradation can reduce the availability of the ethanol-soluble fractions if they are exposed to rumen microflora for more than 2 hours. An oral drench is prepared by dispersing the API at 5.0–8.0 wt% in a propylene glycol and purified water base with 0.2% w/v sodium benzoate and citric acid to pH 5.5–6.0. The mixing vessel is a high-shear overhead mixer operated at 1,500–2,000 rpm for 25–30 minutes; if the batch temperature exceeds 45 °C, the polysaccharide fraction gels and the in-line 100 µm strainer becomes fouled, so a jacketed vessel with 15 °C chilled water is used. After mixing, the liquid is passed through a 100 µm strainer and filled at 100–250 mL into 500 mL HDPE bottles or 100 mL single-use drench vials. The liquid dosage form is tested for microbial enumeration via Ph. Eur. 2.6.13, with a specification of total aerobic microbial count not exceeding 10³ CFU/g and total combined yeast and mold count not exceeding 10² CFU/g; absence of Escherichia coli per Ph. Eur. 2.6.13 is mandatory because the oral drench is often administered to periparturient cows in a barn environment. Impurity profiling follows VICH GL18 for potential degradation products arising from the extraction process; if the API is derived from an ethanol extract, residual ethanol in the finished drench must not exceed 0.5% v/v and is controlled by gas chromatography with headspace injection. Batch retention time at 20–25 °C should be limited to 48 hours before filling because the non-preserved aqueous phase supports fermentative darkening at a pH above 6.5.
Wet granulation of the API for equine feed top-dress produces a free-flowing granule with a tendency to clump if the drying endpoint is set by residual moisture alone. The API is included at 15–25 wt% of the finished granule blend, and the daily dose is 10–20 g per 500 kg body weight. The granulation liquid is a 30% ethanol-water solution added at 8–12% w/w of the dry powder mass in a high-shear granulator; impeller speed is held at 1,200–1,500 rpm for 3–5 minutes, followed by a 1.5 mm conical mill wet sizing. Fluid-bed drying uses inlet air 35–40 °C for 45–60 minutes, with final moisture of 3.0–4.2%; a forced-air oven at 50 °C should be avoided because the outer crust forms a diffusion barrier that leaves core moisture above 6% and causes mold growth in the bulk pack. The dried granules are passed through a 500 µm to 1.18 mm oscillating screener, and fines below 180 µm are recycled only if they constitute less than 10% of the batch. Compliance for equine oral granules is anchored to the European Pharmacopoeia general monograph for granules and to the FEI Clean Sport Prohibited Substances List if the product is intended for competition horses; every batch must be screened for boldenone-like plant sterols and for the presence of undeclared alkaloid markers using LC-MS/MS. The terminal pack is a 2.5 kg bucket or 10 kg bag with a calibrated 20 g scoop, sealed with a foil membrane and stored at or below 25 °C.
| Scenario | Primary compliance anchor | Test parameter | Limit or action |
|---|---|---|---|
| Swine medicated premix | Commission Regulation (EU) 2019/4 Annex II | Homogeneity by ISO 6497:2020 | CV ≤5%; moisture ≤4.5% |
| Injectable solution | Ph. Eur. 2.6.1, Ph. Eur. 2.9.22 | Sterility; bacterial endotoxin | Sterile; ≤0.2 EU/mg |
| Poultry water-soluble powder | EU GMP Part II; Ph. Eur. 2.9.12 | Granule size distribution | 100–212 µm; dispersion stable 30 min |
| Companion-animal tablet | USP 1216, USP 701 | Friability; disintegration | ≤0.8%; ≤30 min |
| Ruminant oral drench | Ph. Eur. 2.6.13; VICH GL18 | Microbial enumeration; impurities | TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g |
| Equine feed top-dress granules | European Pharmacopoeia general monograph for granules; FEI Clean Sport list | Residual moisture; prohibited substance screening | 3.0–4.2%; LC-MS/MS negative |
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Jianji Powder Veterinary Grade API is supplied as an excipient-free, non-sterile bulk powder for further pharmaceutical processing into tablets, injections, capsules, powders, granules, premixes, and solutions. The manufacturer’s product designation is Jianji Powder VG-API, with route-oriented sub-lots identified as VG-T for oral solid dosage forms, VG-I for injectable and solution applications, and VG-P for feed premixes and oral powders. Each sub-lot is released against a separate specification for particle size distribution, bulk and tapped density, loss on drying, assay, related substances, residual solvents, endotoxin, and microbial enumeration. The material is not a feed-grade crude chemical; it is processed under veterinary cGMP with batch-level identity, purity, and impurity control.
Jianji Powder is a manufacturer-designated veterinary API rather than a compendial monograph title. The release criteria below are supplier specifications and are not automatically transferable to other sources of the same active moiety. Batches intended for aqueous injection are controlled for low endotoxin and sub-visible particle burden, whereas premix lots are controlled primarily for blend uniformity, sieve profile, and dusting tendency. Published data for this specific product configuration is limited; the numerical limits in this document are release specifications commonly encountered in multi-route veterinary API supply and are verified by the manufacturer’s quality unit according to ISO/IEC 17025 test procedures.
Jianji Powder VG-T is released with a laser-diffraction particle size distribution controlled to Dv90 ≤ 250 µm and Dv50 75–150 µm. For directly compressible tablet formulations, the compressibility index and Hausner ratio are evaluated using Ph. Eur. 2.9.36 and USP <1174>. Batches with a compressibility index above 25% are routed to wet granulation because they exhibit poor die fill and cohesion on rotary presses. On a 16-station rotary tablet press with 9 mm flat-faced tooling, capping was observed when fines below 45 µm exceeded 30% w/w. The defect was corrected by sifting the powder through a 250 µm vibratory sieve before blending and by adding pregelatinized starch at 3.0% w/w as a dry binder.
For capsule filling, the VG-T sub-lot is specified with bulk density 0.40–0.60 g/mL and tapped density 0.50–0.75 g/mL to permit consistent tamping on dosator-type capsule machines. When tapped density falls below 0.45 g/mL, fill weight variability in low-dose capsules can exceed ±5%. Flow through a 10 mm orifice is also controlled; the discharge rate should exceed 8 g/s for high-speed filling. These density and flow parameters are more restrictive than those applied to VG-P premix powder because capsule and tablet processes require tighter weight uniformity.
Low moisture is a critical boundary for oral solid processing. Loss on drying is controlled to ≤ 1.0% by Ph. Eur. 2.2.32. Batches above 1.0% moisture exhibit increased sticking to tablet punches and uneven granule drying. If the relative humidity in the processing suite exceeds 60%, pre-drying at 40–50 °C for 8–12 h under vacuum is applied before weighing. The powder should not be blended with alkaline excipients unless compatibility screening has been completed, because excessive local pH can accelerate hydrolysis of acid-sensitive active moieties in the presence of residual moisture.
Jianji Powder VG-I is not terminally sterilized and is not supplied as an injectable finished product. The sub-lot is a low-bioburden API intended for sterile filtration during pharmaceutical compounding. The specification requires bacterial endotoxin <0.25 EU/mg by Ph. Eur. 2.6.14 using a validated limulus amebocyte lysate method, and total aerobic microbial count ≤ 10² cfu/g. These limits are lower than those for oral solid and premix sub-lots because endotoxin is not reliably removed by 0.22 µm filtration alone.
Particle size control for injectable use is assigned at Dv90 ≤ 15 µm with no coarse particles above 45 µm. Larger particles reduce filter capacity and can cause premature blinding of sterile filter membranes. The recommended filtration train consists of a 0.45 µm clarifying membrane followed by a 0.22 µm polyethersulfone sterilizing filter. The dried powder should not be autoclaved unless stability data for the specific batch are available; steam sterilisation above 70 °C is outside the typical thermal boundary for the untreated API.
For solution formulations, the powder is dissolved or dispersed in a co-solvent system validated by HPLC assay after 30 min stirring at 20–25 °C in a pH 6.8 phosphate buffer. Batches with surface moisture above 0.5% should be dried before aqueous solution preparation because hydrolysis can reduce assay and increase related substances. The material should not be co-milled with alkaline buffers or amine-based additives unless specific compatibility data are available.
In process operations, the VG-I sub-lot is packaged in double polyamide-lined aluminium foil bags under nitrogen. Batch-to-batch variance in residual moisture is controlled to ≤ 0.5%, and the headspace oxygen in primary packaging is verified below 2% for oxidatively unstable actives. These controls are not required for VG-P premix powder, which is packaged in standard fibre drums with a polyethylene liner.
Wet granulation changes the flow and compressibility profile of Jianji Powder VG-T. In a high-shear granulator with impeller tip speed 5–10 m/s and chopper speed 1000–1500 rpm, the powder is granulated with purified water or binder solution to a target loss on drying of 1.5–2.5%. Drying in a fluid-bed dryer at 50–60 °C continues until loss on drying is ≤ 2.0%. Overdrying below 1.0% can produce friable granules that generate fines during subsequent compression. Overwetting above 3.0% causes granule agglomeration and uneven die filling. The granulated material is passed through a 850 µm screen before final blending.
For premix and oral powder applications, the VG-P sub-lot uses a coarser particle size profile: Dv90 ≤ 355 µm, with no more than 10% w/w retained on a 500 µm sieve. This profile is selected because very fine material increases dusting and segregation in ribbon mixers and double-shaft paddle mixers. Blend uniformity is tested according to Ph. Eur. 2.9.40; the release criterion for active concentration is 90.0–110.0% of label claim across 10 sampling points. If the carrier is non-porous, the powder can be blended directly; if the carrier is hygroscopic, pre-drying of the carrier is required before addition of the API.
Dusting tendency is assessed on a vibratory sieve stack and by measuring airborne dust during a 5 min transfer trial. The VG-P sub-lot is not intended for direct parenteral use and carries a higher endotoxin limit than VG-I. Nonetheless, microbial enumeration is specified and tested by Ph. Eur. 2.6.12, with total aerobic microbial count ≤ 10³ cfu/g and total yeast and mould count ≤ 10² cfu/g.
In medicated feed production, the powder is often used at inclusion rates below 1 kg/tonne. At these levels, the carrier particle size and electrostatic charge dominate blend consistency. The VG-P sub-lot is therefore controlled for bulk density 0.35–0.70 g/mL and moisture ≤ 1.0% to minimise stickiness during screw conveying. Batches that exceed 1.0% moisture should be re-dried before mixing to prevent adherence to ribbon mixer blades and transfer piping.
Tablet, capsule, and granule usage of Jianji Powder requires a narrower particle size window than premix usage. The VG-T sub-lot is assigned to oral solid dosage forms, while VG-P is assigned only to oral powders and feed premixes. If a batch originally designated VG-P is considered for tablet manufacture, it must be re-milled and re-tested against the VG-T particle size and flow specification. This route-oriented release system is a key difference from single-grade veterinary powders that use one specification for all applications.
| Attribute | VG-T / oral solid | VG-I / injectable and solution | VG-P / premix and oral powder | Test method |
|---|---|---|---|---|
| Particle size Dv90 | ≤ 250 µm | ≤ 15 µm | ≤ 355 µm | Ph. Eur. 2.9.35 / USP <429> |
| Bulk density | 0.40–0.60 g/mL | 0.20–0.50 g/mL | 0.35–0.70 g/mL | Ph. Eur. 2.9.34 |
| Loss on drying | ≤ 1.0% | ≤ 0.5% | ≤ 1.0% | Ph. Eur. 2.2.32 |
| Assay on anhydrous basis | 98.0–102.0% | 98.0–102.0% | 98.0–102.0% | HPLC Ph. Eur. 2.2.29 |
| Bacterial endotoxin | <1.0 EU/mg | <0.25 EU/mg | <5.0 EU/mg | Ph. Eur. 2.6.14 |
| Total aerobic microbial count | ≤ 10³ cfu/g | ≤ 10² cfu/g | ≤ 10³ cfu/g | Ph. Eur. 2.6.12 |
| Total yeast and mould count | ≤ 10² cfu/g | ≤ 10¹ cfu/g | ≤ 10² cfu/g | Ph. Eur. 2.6.12 |
| Residual solvents | ICH Q3C class 1 not detected; class 2 within limits | ICH Q3C class 1 not detected; class 2 within limits | ICH Q3C class 1 not detected; class 2 within limits | GC-HS Ph. Eur. 2.4.24 |
Route-specific specifications are applied at batch release, but the active moiety itself remains the same. The differences among VG-T, VG-I, and VG-P are physical and microbiological rather than chemical. This design reduces the need for terminal reprocessing at the pharmaceutical manufacturer. However, the API purchaser remains responsible for confirming suitability for the intended finished product and for validating each downstream formulation.
| Property | Jianji Powder VG-API | Feed-grade raw powder |
|---|---|---|
| Particle size control | Route-specific Dv90 and sieve limits | Wide distribution without Dv90 control |
| Endotoxin | Tested and limited per route | Not routinely tested |
| Residual solvents | ICH Q3C class 1 and class 2 controlled | Often not controlled |
| Microbial enumeration | Specified cfu/g limits | Absent or high limits |
| Documentation | Full certificate of analysis with ISO/IEC 17025 methods | Basic purity or composition only |
| Intended use | Tablets, injections, capsules, powders, granules, premix, solutions | Technical or feed use only without pharmaceutical release |
The VG-I sub-lot differs from VG-T and VG-P primarily in endotoxin burden, particle size, and residual moisture. Mixing sub-lots is not permitted because a VG-I batch can be disqualified for parenteral use if it is blended with unmicronized oral-grade material. Similarly, a VG-T batch should not be re-labelled as VG-I without passing the full parenteral release specification. These boundary controls are required because the powder is supplied as an unformulated API, and the downstream dosage form influences the critical quality attributes of the substance.