| HS Code | 117748 |
| Product Name | Sanhuang Shuangding Powder Veterinary Grade API |
| Product Type | Veterinary Herbal Extract Active Pharmaceutical Ingredient |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Active Ingredients | Coptis chinensis extract, Scutellaria baicalensis extract, Phellodendron amurense extract, Taraxacum officinale extract, Viola yedoensis extract |
| Appearance | Yellowish-brown to brown powder |
| Odor | Characteristic herbal odor with a slight bitter taste |
| Solubility | Partially soluble in water; forms a uniform suspension when stirred |
| Pathogenic Bacteria | Salmonella negative in 10 g; Escherichia coli negative in 10 g |
| Pharmacological Action | Heat-clearing, detoxifying, anti-inflammatory, antibacterial, and anti-endotoxic |
| Indications | For veterinary prevention and treatment of bacterial and viral infections, inflammatory conditions, and fever |
| Storage Conditions | Sealed, cool, dry, well-ventilated area; protected from light, moisture, and high temperature |
| Shelf Life | 24 months under recommended storage conditions |
| Packaging | Double polyethylene bags inside; outer aluminum foil bag or sealed container |
| Quality Grade | Veterinary grade API suitable for further pharmaceutical manufacturing |
As an accredited Sanhuang Shuangding 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 sealed, light-resistant containers. Net weight 25 kg per drum, labeled for veterinary API use. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Sanhuang Shuangding veterinary API packed in sealed drums/cartons, palletized, secured, moisture-proof, ventilated, compliant shipping. |
| Shipping | Sanhuang Shuangding Powder Veterinary Grade API ships as a dry, sealed, moisture-protected powder in tamper-evident containers. Ensure temperature-controlled, dry handling within 24 hours. Include Material Safety Data Sheets, Certificate of Analysis, and comply with international veterinary drug transport regulations to prevent contamination or degradation during transit. |
| Storage | Store in a tightly sealed, original container in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, and high temperatures. Keep away from incompatible substances and food. Ensure container remains closed when not in use. Follow veterinary pharmacopeial guidelines; use within stated shelf life. |
| Shelf Life | Shelf life is 24 months when stored sealed in a cool, dry place, protected from moisture and light. |
When a heat-labile botanical powder is formulated as a drinking-water-soluble granule for poultry flocks, the controlling variable is not beaker dissolution speed but coefficient of variation across nipple-drinker lines after stock-solution mixing in proportioner medicators. The milled Sanhuang Shuangding Powder is pre-blended with anhydrous dextrose or low-moisture lactose until the finished granule carries 15–35% w/w active powder; the granulation step occurs in a high-shear mixer with 2–3% w/w PVP K30 binder dissolved in purified water, and the wet mass is passed through an ASTM E11 No. 18 mesh screen before fluid-bed drying at inlet air 55–65 °C. Drying above 65 °C reduces the recoverable alkaloid fraction and increases friable fines; drying below 55 °C leaves residual moisture above 3.0% and causes clumping in aluminium-foil sachets. After reconstitution, the stock solution is fed through dosing medicators at 1:128; the pH is adjusted to 4.5–6.5 with citric acid/sodium citrate because the un-ionized alkaloids precipitate above pH 7.5 and block narrow drinker nipples. Compliance for this route is assessed under Ph. Eur. 5.1.4 and Ph. Eur. 2.9.5; in the EU, the finished medicated drinking-water product falls under Regulation (EU) 2019/6, and the API dossier follows VICH GL18 residual-solvent limits where applicable. Finished forms are 50 g, 100 g, and 500 g foil-lined sachets or HDPE jars with an in-use shelf life of 24 h after reconstitution at 20–25 °C.
Terminal sterilization of a clarified botanical extract is not a simple 121 °C cycle; the same alkaloid species that provide antimicrobial activity degrade through oxidative cleavage when exposed to steam for periods exceeding F0 ≥ 12. The crude API is first dispersed in Water for Injection at 1:8–1:15 w/v and extracted at 60 °C for 1 h; after centrifugation at 12,000 ×g, activated carbon at 0.05% w/v is used to strip endotoxin and high-molecular-weight pigmented proteins, followed by staged filtration through 0.45 μm PES and 0.22 μm PVDF membranes. The clarified solution is adjusted to 10–25 mg/mL total solids and filled into 10 mL, 20 mL, and 50 mL amber Type I glass vials under Grade B or Grade C cleanroom with Grade A filling line conditions per ISO 14644-1; amine buffers such as tris are avoided because they raise pH above 7.5 and precipitate the alkaloid fraction. Published degradation kinetics for this specific multicomponent powder are limited; therefore the sterilization load is bracketed by marker retention rather than by fixed time-temperature extrapolation. Compliance endpoints include Ph. Eur. 2.6.1 sterility, Ph. Eur. 2.6.14 bacterial endotoxins, and Ph. Eur. 2.9.19 particulate matter. This route is limited to intramuscular or subcutaneous injectable solutions; intravenous use is not assigned unless pyrogen burden and particulate load are validated in target species.
Where the powder is assigned to a Type A medicated article for incorporation into compound feed, the batch-to-batch carryover risk is controlled by sequencing the mill after a 5 kg pre-flush of unmedicated carrier rather than by extending mixer time alone. Premix production uses a double-ribbon mixer with working capacity 500–2,000 kg, mixing time 8–12 min at 25 rpm, and coefficient of variation ≤7% using the sampling protocol of ISO 6497:2002. API addition in the premix is 5–25% w/w, with corncob meal, rice hull, or calcium carbonate carrier to bring final feed concentration to 500–2,000 mg/kg when applied at 2–10 kg/tonne. Steam conditioning behind a paddle conditioner is maintained at 70–75 °C for 30–45 s; thermal input above 80 °C accelerates browning and lowers recoverable marker alkaloids. If the veterinary premix is pelleted, post-pelleting liquid spraying of the liquid extract is preferred over pre-pelleting powder injection because of the higher surface-temperature exposure on the die. Compliance under Regulation (EC) No 183/2005, Regulation (EU) 2019/4, and Directive 2002/32/EC; the US route follows 21 CFR Part 507 and medicated feed regulations in 21 CFR Part 558. Terminal products are 5 kg and 25 kg multi-wall paper bags with inner PE liner, intended for feed-mill or on-farm mixing.
| Downstream format | Primary standard | Test method / endpoint | In-process limit |
|---|---|---|---|
| Water-soluble granules | Ph. Eur. 5.1.4 | Ph. Eur. 2.9.5 mass uniformity; Ph. Eur. 2.2.32 loss on drying | Residual moisture ≤3.0%; pH 4.5–6.5 |
| Injectable solution | Ph. Eur. 5.1.1 sterile products | Ph. Eur. 2.6.1 sterility; Ph. Eur. 2.6.14 endotoxin; Ph. Eur. 2.9.19 particulate | Endotoxin ≤0.5 EU/mL for non-IV; filter integrity ≥3,000 mbar |
| Feed premix | Regulation (EC) No 183/2005 | ISO 6497:2002 sampling; mixer CV ≤7% | Premix addition 5–25% w/w; final feed 500–2,000 mg/kg |
| Bolus/tablet | Ph. Eur. 5.1.4 | USP <1216> friability; USP <905> weight variation | Hardness 60–100 N; friability ≤1.0% |
| Capsule | Ph. Eur. 5.1.4 | Ph. Eur. 2.9.5; USP <905> | Fill weight 250 mg or 500 mg; ≤35% RH |
| Oral drench | Ph. Eur. 5.1.4 | Ph. Eur. 2.6.13 specified microorganisms | pH 5.5–6.5; entrained air ≤0.5% v/v |
Direct compression of a high-fiber botanical API into 2–10 g bovine and equine boluses faces a narrow processing window: if blend moisture exceeds 3.5%, capping occurs; if compression force exceeds 20 kN, disintegration times lengthen beyond 30 min because the alkaloid-rich granulate undergoes plastic deformation under high dwell time. The formulation uses 35–65% w/w API, 30–45% w/w microcrystalline cellulose, 2–5% w/w crospovidone, 0.5–1.5% w/w magnesium stearate, and 0.5–1.0% w/w colloidal silicon dioxide. The powder is dried to ≤3% moisture in a tray dryer at 40 °C, blended for 10 min, and compressed on a rotary tablet press with 16 stations, precompression 4–8 kN, main compression 12–18 kN, and turret speed limited to 20–30 rpm because higher speeds increase lamination caused by entrapped air in the high-fiber blend. Hardness is maintained between 60–100 N; friability below 1.0% per USP <1216>; weight variation per USP <905>. Compliance includes Ph. Eur. 5.1.4 and EU Regulation (EU) 2019/6. Terminal product types are immediate-release 2 g, 5 g, and 10 g boluses or tablets for cattle, calves, and equine patients.
Hard capsule filling of the milled API is limited by its bimodal particle-size distribution; without a 0.5% silica flow aid the powder’s angle of repose exceeds 45°, causing frequent dosator pin blockages on rotary filling machines. The capsule blend is composed of 70–90% w/w API, 10–25% w/w pregelatinized starch, 0.5% w/w magnesium stearate, and 0.5% w/w colloidal silicon dioxide; the fill weight is 250 mg or 500 mg into size 0 or size 1 HPMC capsules. Filling rooms are maintained at ≤35% RH to prevent HPMC shell swelling and powder coating of the dosing pins. Compliance uses uniform mass and content uniformity tests under Ph. Eur. 2.9.5 and USP <905>; the finished veterinary capsule is a 24-count or 60-count HDPE bottle for companion animals.
Oral drench solutions require a low-viscosity but yield-stable suspension; the API is dispersed in purified water at 5–15% w/v with 0.2–0.5% xanthan gum to prevent needle settling in automatic drenching guns. The vehicle is prepared by hydrating xanthan gum under high shear at 1,500–2,000 rpm for 20 min, then the API is added through an in-line rotor-stator and homogenized at 3,000 rpm; the suspension is deaerated under vacuum and adjusted to pH 5.5–6.5 with citrate buffer. Freezing is avoided because repeated freeze-thaw cycles cause irreversible aggregation of the polysaccharide suspended solids and clog the drench-gun check valves. Aeration during mixing must be controlled below 0.5% v/v entrained air to prevent dose-volume error in automatic equipment. Compliance is set by Ph. Eur. 5.1.4 for non-sterile liquids and Ph. Eur. 2.6.13 for specified microorganisms; terminal product types are 1 L and 5 L HDPE drench packs for cattle, sheep, and goats.
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Sanhuang Shuangding Powder is supplied as a spray-dried or vacuum-dried multicomponent botanical API powder for downstream conversion into tablets, injections, capsules, powders, granules, premixes, and solutions. Two veterinary-grade API models are available: SHSD-P-VG-API-100 for injection-grade applications and SHSD-P-VG-API-200 for oral and feed-premix applications. The powder is standardised to HPLC marker compounds rather than to a single extraction solvent signature; the release basis comprises total anthraquinones, berberine hydrochloride, and baicalin, with representative limits of total anthraquinones not less than 1.0% w/w, berberine hydrochloride not less than 0.5% w/w, and baicalin not less than 2.0% w/w. Physical presentation is a brownish-yellow to brown hygroscopic powder with a bulk density of 0.35–0.55 g/mL and a tapped density of 0.50–0.75 g/mL. The injection-grade model is controlled to a particle-size distribution of D90 ≤ 30 µm, while the oral-grade model is controlled to D90 ≤ 180 µm. The product retains the natural botanical matrix; therefore, aqueous preparations are colloidal dispersions rather than true solutions, and this characteristic governs downstream filtration, filling, and sterilisation choices.
| Parameter | SHSD-P-VG-API-100 injection-grade | SHSD-P-VG-API-200 oral/feed-premix |
|---|---|---|
| Appearance | Brownish-yellow to brown powder | Brownish-yellow to brown powder |
| Particle size | D90 ≤ 30 µm | D90 ≤ 180 µm |
| Loss on drying | ≤ 5.0% w/w | ≤ 5.0% w/w |
| Total ash | ≤ 8.0% w/w | ≤ 8.0% w/w |
| Heavy metals | ≤ 10 ppm | ≤ 20 ppm |
| Arsenic | ≤ 2 ppm | ≤ 2 ppm |
| Escherichia coli | Absent in 1 g | Absent in 1 g |
| Salmonella | Absent in 10 g | Absent in 10 g |
| Total aerobic microbial count | ≤ 10 CFU/g | ≤ 1000 CFU/g by USP <61> |
| Combined yeast and mould count | ≤ 10 CFU/g | ≤ 100 CFU/g by USP <61> |
| Bacterial endotoxins | ≤ 0.5 EU/mg by USP <85> | Not specified |
| Residual solvents | ICH Q3C: ethanol ≤ 5000 ppm | ICH Q3C: ethanol ≤ 5000 ppm |
Process data from production-scale spray drying on a 200 L rotary-atomiser dryer with inlet air at 160–170 °C and outlet temperature maintained at 70–75 °C indicate that the moisture endpoint is sensitive to outlet air temperature. Above 75 °C, the marker compounds baicalin and berberine hydrochloride show HPLC area losses exceeding 2–3% relative to the input extract solids; below 68 °C, residual moisture rises above 5.0% w/w and powder caking occurs on the cyclone wall. The spray-dried powder exhibits an onset glass transition near 55 °C by modulated differential scanning calorimetry; therefore, milling and sieving are performed with nitrogen cooling to keep the powder below 45 °C. The injection-grade model is further processed through a spiral jet mill with nitrogen cooling to achieve D90 ≤ 30 µm. The milled powder is then sieved through an inline vibratory sieve with a 150 µm mesh for the oral model and a 45 µm mesh for the injection model. Bulk density after milling is maintained at 0.38–0.48 g/mL to support capsule filling and tablet die fill consistency. For aqueous reconstitution, the injection-grade powder is dispersed under high-shear mixing at 3000 rpm for 10 min; undissolved matrix solids are removed by centrifugation at 8000 rpm before sterile filtration. The resulting filtrate remains opalescent, and light obscuration testing should be used to confirm particulate matter limits for injectable finished products.
For dry premix and granule manufacture, the oral-grade powder is commonly adsorbed onto precipitated silica or maltodextrin at a ratio of 1:4 to 1:9 to reduce segregation and improve flow. In a 500 L ploughshare mixer run at 60 rpm for 10 min, blend uniformity values of ≤ 5.0% RSD are obtained when the API is pre-milled to D90 ≤ 180 µm; coarser material shows content uniformity failures in low-dose tablets where the API component is below 2.0% w/w of the tablet mass. Moisture uptake is a critical limit: the powder is hygroscopic and may gain 1.5–2.5% w/w moisture within 30 min at 25 °C and 60% RH. Therefore, open handling is limited to ≤ 30 min in non-conditioned cleanrooms; pre-drying is required when the powder is stored at RH > 60% or when the residual water by USP <921> exceeds 6.0% w/w. Wet granulation is performed with an aqueous binder solution containing polyvinylpyrrolidone at 3–5% w/w; the wet mass is dried in a fluid-bed dryer at inlet air temperature not exceeding 60 °C to avoid thermal marker loss. Granules for premix use are typically sized through a 1.0 mm screen and blended with ground corn cob or dextrose to a final API concentration of 0.1–1.0% w/w depending on the target species and dosing programme. Finished premixes are assayed after 10 random sampling points; acceptance is 90.0–110.0% of label claim with RSD ≤ 5.0%.
The injection-grade specification differs not only by particle size but by bacterial endotoxin, bioburden, and particulate matter controls. The oral-grade powder may carry a total aerobic microbial count of ≤ 1000 CFU/g and a combined yeast and mould count of ≤ 100 CFU/g when tested according to USP <61>; this is acceptable for dry oral dosage forms but is not acceptable for injection. The injection-grade model is controlled to ≤ 10 CFU/g total aerobic microbial count, and bacterial endotoxins are not more than 0.5 EU/mg by USP <85>. Terminal sterilisation of the finished solution is still required; the API is not sterilised as a dry powder in routine production. Particulate matter is controlled after reconstitution through a 0.45 µm clarifying filter and a 0.22 µm sterilising-grade membrane. The multi-herb matrix contains water-insoluble polysaccharides and tannins; therefore, the injection model is extracted through a sequence of ethanol precipitation, centrifugation at 8000 rpm, and membrane clarification to reduce insoluble solids before spray drying. Residual ethanol after drying is controlled under ICH Q3C at ≤ 5000 ppm; acetone and methanol are not used in the injection-grade extraction path.
When the spray-dried powder is directed to tablet compression, a 16-station rotary tablet press equipped with 8 mm round tooling is used. Blends containing the API at 5–30% w/w with microcrystalline cellulose and croscarmellose sodium compress at 8–15 kN to produce tablets with hardness 60–120 N and friability below 1.0% w/w by USP <1216>. Disintegration tested by USP <701> is ≤ 15 min in water at 37 °C for uncoated tablets. Because the powder contains hygroscopic botanical solids, prolonged dwell times above 20 ms at RH > 50% may cause picking on the upper punch face. Capsule filling on a dosator machine with size 0 capsules requires a minimum bulk density of 0.40 g/mL and a maximum angle of repose of 38°; when the powder is milled too fine, flow aids such as fumed silica at 0.5–1.0% w/w are necessary. Powder formulations for direct administration are adjusted to a target marker content through geometric dilution with dextrose or lactose; the final powder should be protected from light and moisture in unit-dose sachets.
Unlike non-API feed-grade botanical powders, this product is released under pharmacopoeial microbial, heavy metal, and marker-content controls and is supported by batch-specific certificates of analysis. Unlike single-compound synthetic APIs, the Sanhuang Shuangding Powder API is a multi-component matrix whose clinical effect, where described, derives from a defined marker profile rather than a single chemical entity. This difference influences analytical strategy: release testing requires simultaneous HPLC separation of anthraquinone, isoquinoline alkaloid, and flavone fractions with relative retention time matching against certified reference substances. For some single-marker equivalence studies, published data for this specific configuration is limited; therefore, formulation decisions should be confirmed by pilot-scale trials using the intended final dosage form.
| Parameter | Sanhuang Shuangding Veterinary API | Non-API feed-grade botanical powder | Single-compound synthetic API |
|---|---|---|---|
| Standardisation basis | Multi-marker HPLC; total anthraquinones ≥ 1.0% w/w, berberine HCl ≥ 0.5% w/w, baicalin ≥ 2.0% w/w | Visual identity, foreign matter, moisture | Single assay with purity by HPLC/GC |
| Microbial control | USP <61>/<62>; oral ≤ 1000 CFU/g; injection ≤ 10 CFU/g; endotoxin ≤ 0.5 EU/mg for injection | Variable total plate count; no endotoxin control | Specified only for sterile bulk where required |
| Particle-size control | Injection D90 ≤ 30 µm; oral D90 ≤ 180 µm | Coarse or variable | Milled crystalline distribution controlled by manufacturer |
| Residual solvent control | ICH Q3C; ethanol ≤ 5000 ppm | Not controlled | ICH Q3C |
| Dosage-form breadth | Tablets, injections, capsules, powders, granules, premixes, solutions | Feed premix only | Dependent on solubility and stability |
Steam sterilisation at 121 °C for 15 min is feasible only if the batch has been validated for pH stability and marker retention. The solution pH should be maintained between 5.5 and 6.8; above pH 7.5, berberine hydrochloride precipitates, and below pH 3.5, baicalin solubility decreases. In heat-sensitive formulations, aseptic processing through a 0.22 µm sterilising-grade polyethersulfone filter is used; filter compatibility studies show that nylon membranes may adsorb anthraquinones and should be avoided. The maximum holding time of the compounded solution before filtration is 4 h at 20–25 °C under nitrogen blanketing; longer holding times lead to visible particulate formation. The powder should not be dry-autoclaved, and it should not be blended with amine-based preservatives that can generate aldehydes under terminal heat. For injectable manufacturing, the API is reconstituted in water for injection at 20–25 °C, adjusted to pH 5.8–6.2, prefiltered through a 0.45 µm polypropylene cartridge, and then sterile-filtered into sterilised depyrogenated vials. Terminal sterilisation by autoclave is selected only when the finished solution remains within the marker-content specification after the cycle.
For all models, the primary packaging is a double polyethylene liner inside an aluminium foil laminate bag, with 25 kg net per drum. Storage is at ≤ 25 °C and ≤ 60% RH in a light-protected area; freezing is not recommended. The manufacturer’s retest period is 24 months for unopened oral-grade material and 18 months for injection-grade material. Once opened, the powder should be used within 30 days when stored under nitrogen. Avoid contact with strong oxidising agents, acidic materials that may hydrolyse flavonoid glycosides, and open handling during high-humidity seasons without dehumidification. If a batch exceeds the specified residual water limit of 6.0% w/w by USP <921>, re-drying at 50 °C under vacuum is permitted only for oral-grade material; injection-grade material should not be re-dried because of endotoxin redistribution and particle-surface changes. The packaging is not suitable for aseptic transfer; injection-grade material is subdivided into single-use gamma-sterilised pouches when required.