| HS Code | 667045 |
| Product Name | Siwu Decoction Powder Veterinary Grade API |
| Product Category | Traditional Chinese Veterinary Medicine Active Pharmaceutical Ingredient |
| Dosage Form Compatibility | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Active Pharmaceutical Ingredients | Angelicae Sinensis Radix, Ligustici Chuanxiong Rhizoma, Paeoniae Radix Alba, Rehmanniae Radix Praeparata |
| Key Marker Compounds | Ferulic acid, paeoniflorin, ligustilide, catalpol |
| Appearance | Brown to brownish-yellow powder with characteristic odor and slightly sweet-bitter taste |
| Solubility | Partially soluble in hot water; forms a colloidal suspension in cold water |
| Ph Of 1 Aqueous Suspension | 4.0 to 6.5 |
| Storage Condition | Keep sealed in a cool, dry, well-ventilated place; protect from light and moisture |
| Shelf Life | 24 months under recommended storage conditions |
| Pharmacological Properties | Supplements blood, promotes blood circulation, regulates liver function, modulates immune response, and supports reproductive health |
| Veterinary Target Species | Cattle, sheep, goats, pigs, poultry, horses, dogs, and cats |
As an accredited Siwu Decoction 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, moisture-proof aluminum foil bags, 25 kg net weight per bag, labeled for veterinary grade API use. |
| Container Loading (20′ FCL) | 20′ FCL loading: Siwu Decoction Powder Veterinary Grade API, in sealed drums/cartons, palletized and secured for safe, dry transport. |
| Shipping | Shipping: Packed in sealed, moisture-proof pharmaceutical-grade drums to preserve stability. Requires cool, dry, well-ventilated conditions, away from direct sunlight. Shipments comply with veterinary API regulations, with temperature-controlled options available. Offer global express, air, or sea freight with full documentation and tracking. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature (below 25°C). Keep the container tightly sealed, protected from light, moisture, and direct sunlight. Avoid exposure to humidity and strong odors. Maintain original packaging until use, with appropriate handling for veterinary formulations. Keep out of reach of children and animals. |
| Shelf Life | Shelf Life: 24 months from manufacture date when stored in sealed, original containers in a cool, dry place. |
Dispersion of Siwu Decoction Powder Veterinary Grade API into drinking-water formulations is governed by the water-extractable polysaccharide fraction and the particle-size distribution of the dried extract. The material is hygroscopic and forms cohesive aggregates when ambient relative humidity exceeds 60% RH; therefore, pre-blending with hydrous lactose monohydrate at a 1:3 to 1:5 ratio is required before the API enters the final blender. A 400 L ribbon blender operated at 15–20 rpm with 60–70% working volume provides sufficient shear to break extract agglomerates without generating excessive fines. Colloidal silicon dioxide is added at 0.5–1.0 wt% as a moisture scavenger and flow aid, and sodium lauryl sulfate is incorporated at 0.5 wt% to improve rewetting when the finished powder is added to drinking water. The blend is passed through a 1.0 mm screen and then filled into aluminium foil laminate pouches. The terminal water-soluble oral powder is intended for batch-tank administration to swine and poultry after reconstitution in potable water at 20–25 °C.
Microbiological control for this powder form follows USP <61> for total aerobic microbial count and USP <62> for specified pathogens; the release specification normally sets total aerobic count at not more than 10³ CFU/g and requires absence of Salmonella in 25 g. Loss on drying is controlled by USP <731> at not more than 5.0% because excess free moisture accelerates extract caking during storage. Species-specific dosing is fixed by the approved veterinary dossier, not by this document. A process limitation is that direct addition of the unmixed API into cold water produces gel-like lumps that block nipple-drinker lines; therefore, a pre-slurry step using a 1:10 powder-water dispersion and a high-shear mixer at 1500 rpm for 5 min is required on farm before introduction into the main tank.
Before direct compression is attempted, the API is dried in a forced-air tray dryer at 40 °C for 2 h until loss on drying reaches 4–5%. Higher temperature is not applied because darkening and marker loss occur above 70 °C. The direct compression formulation uses API at 35–50 wt%, microcrystalline cellulose PH102 at 40–55 wt%, crospovidone at 3 wt%, povidone K30 at 2–4 wt%, colloidal silicon dioxide at 0.5 wt%, and magnesium stearate at 0.5–1.0 wt%. The API and all excipients except magnesium stearate are blended in a V-blender at 20 rpm for 15 min; the lubricant is then added and blended for an additional 3 min. Magnesium stearate must not exceed 1.5 wt% because the hydrophobic film retards wetting and prolongs disintegration beyond the release limit.
Compression is carried out on a rotary tablet press with 8 mm flat-faced beveled punches at 30 rpm, with compaction force set between 10 kN and 18 kN. Target tablet hardness is 5–8 kp. At compaction force above 18 kN, capping occurs because the elastic recovery of the dried botanical extract disrupts the compact. Tablets are tested for friability by USP <1216> with a limit of not more than 1.0%, disintegration by USP <701> in purified water at 37 °C with a limit of not more than 30 min, content uniformity by USP <905> with acceptance value not more than 15, and dissolution by USP <711> using apparatus 2 at 50 rpm in 900 mL purified water. The terminal finished product is an uncoated veterinary oral tablet. If the production suite exceeds 60% RH, picking and sticking on punch faces become unavoidable, and the batch is typically rejected due to weight variation before friability testing.
The injectable route exposes the API to three simultaneous process risks: thermal degradation of the paeoniflorin marker, precipitation of high-molecular-weight polysaccharides, and endotoxin carry-over from botanical raw material. The service form is prepared as an aqueous solution buffered to pH 5.0–6.5; below 4.5, acid hydrolysis of glycosidic bonds accelerates, and above 6.8, polyphenol oxidation produces visible darkening. Terminal sterilization at 121 °C for 15 min is acceptable only when marker retention is not less than 95% and pH drift is not more than 0.2 units. If these limits are not met, the batch is sterile-filtered through a 0.45 µm PVDF prefilter and then a 0.22 µm polyethersulfone membrane under Grade A conditions in a ISO 14644-1 Grade B background. To reduce polysaccharide flocculation during storage, the bulk solution may be ultrafiltered through a 10 kDa MWCO polyethersulfone cassette before final dilution; paeoniflorin and ferulic acid permeate, while higher-molecular-weight extract components remain in the retentate.
| Quality Attribute | Method/Standard | Release Limit |
|---|---|---|
| pH | USP <791> | 5.0–6.5 |
| Bacterial endotoxins | USP <85> | ≤0.5 EU/mg of anhydrous extract |
| Particulate matter | USP <788> | meets small-volume injection limits for containers ≤ 100 mL |
| Sterility | USP <71> | no growth after 14 days |
| Residual solvents | VICH GL18 | Class 2 solvents not more than Option 1 limits |
The injectable terminal product is a sterile solution filled into Type I borosilicate glass vials and sealed with coated butyl rubber closures. Antioxidant systems used in batch development should avoid amine-based buffering species; Siwu Decoction contains phenolic acids that can form colored amine-phenol complexes. Nitrogen sparging during compounding and headspace purging before stoppering reduce oxidative browning. Published compendial data for this specific parenteral configuration is limited, so marker loading and preservative choice are fixed against the approved veterinary dossier and stability data generated under VICH GL3. If a multi-dose presentation is required, the preservative efficacy must meet USP <51>, but the selection of preservative is species-specific because benzyl alcohol and parabens have differing toxicological limits in cats, dogs, and food-producing species.
Low-moisture capsule filling of the material is carried out at 25–30% RH and 20–22 °C, rather than ambient conditions, to prevent gelatin embrittlement and tackiness. The choice of shell material is a process-critical decision: hard gelatin capsules develop crosslinking because residual reducing sugars in the dried decoction powder can react with gelatin lysine residues under warm, moist storage; therefore, hydroxypropyl methylcellulose capsules are specified for long-duration veterinary products. The powder blend for encapsulation contains API at 200 mg, lactose monohydrate at 180 mg, pregelatinized starch at 20 mg, and talc at 3 mg per capsule, giving a total fill weight of approximately 400 mg. The API is dried to loss on drying not more than 4.0% before blending, and the blend is passed through a 30-mesh screen.
A Bosch GKF series capsule filling machine is operated at 20,000–60,000 capsules/hour depending on material index; tamping pin compression is set between 20 N and 30 N to avoid plug formation and weight segregation. The filled capsules are metal-checked, dedusted, and then tested for disintegration by USP <701> using sinkers in 0.1 N HCl at 37 °C with a limit of not more than 30 min. Dissolution is tested by USP <711> apparatus 2 at 50 rpm in 900 mL 0.1 N HCl. The terminal dosage form is a hard HPMC capsule for oral administration to companion animals or calves; packaging is cold-form aluminium blister under desiccant if the product is distributed to a climate zone exceeding 65% RH mean annual humidity.
A feed premix based on Siwu Decoction Powder Veterinary Grade API is not a simple dilution; it is a carrier-bound dry mixture in which particle-size mismatch and bulk-density difference control assay uniformity. The carrier is selected from ground corn cob #20–#40, rice hulls, or calcium carbonate, with bulk density between 0.35 g/cm³ and 0.50 g/cm³. The API is incorporated at 10–20 wt% using a two-step mixing sequence: first a basal premix is produced at 1:5 API-to-carrier ratio in a 100 L ribbon mixer for 10 min; then this basal premix is let down into the full carrier in a 500 L ribbon mixer at 15 rpm for 20–30 min. Overmixing beyond 35 min can reintroduce assay variation because the denser API-rich particles migrate toward the bottom discharge, while the lighter fibrous carrier stratifies upward. Homogeneity is verified by withdrawing 10 samples at fixed discharge intervals and calculating the coefficient of variation; the acceptance limit is not more than 5% for the marker compound, typically ferulic acid or paeoniflorin by high-performance liquid chromatography using USP <621> principles.
The finished premix is packed into 25 kg or 5 kg multi-wall paper bags with an inner polyethylene liner. Regulatory controls include current feed-industry requirements under EU Regulation 2019/4 for medicated feed intermediates and 21 CFR 225 for medicated feed manufacturing where applicable. If calcium carbonate is used as a carrier, its residual moisture must remain below 8%; a wet carbonate raises the local pH and accelerates degradation of paeoniflorin during ambient storage. The terminal product is a feed premix intended for incorporation at the feed mill into complete feed using a horizontal batch mixer with a validated mixing time. Bulk-carrier mycotoxin status should be verified by the carrier supplier because aflatoxin-controlled feed grade is not automatically granted for all botanical premix applications.
In fluidised-bed processing, the controlling variable shifts from blend uniformity to droplet penetration time and the fracture strength of agglomerates. The API is first dry-blended with corn starch at 20–30 wt% and loaded into a top-spray fluidised-bed granulator. Aqueous hydroxypropyl methylcellulose at 3% w/w is sprayed at 15–30 g/min with inlet air temperature 60–70 °C, atomization air pressure 1.5–2.0 bar, and product temperature held at 35–45 °C. Product temperature above 50 °C produces brittle granules and generates dust; below 30 °C the bed becomes overwet and loses fluidization. The spray interval is paused when the bed moisture reaches the liquid saturation phase, which is detected by an increase in pressure drop across the product retainer and a shift in outlet humidity. After the binder is exhausted, the granules are dried at inlet air 60 °C until loss on drying reaches 3–5%, then passed through a 16–20 mesh oscillating granulator.
The dried granule fraction is suitable for sachet filling, capsule filling, or final repacking as an oral granule. Bulk density is typically controlled between 0.40 g/mL and 0.55 g/mL, and the Carr index is expected to be not more than 25 when measured by ASTM D6393. Particle-size distribution is checked by sieve analysis per ISO 9276-1; material retained above 2.0 mm is rejected because it will not flow uniformly through high-speed sachet form-fill-seal dosing stations. The terminal product is a moisture-protected oral granule packaged in foil sachets under ≤30% RH. If the granulation is intended for premix let-down rather than direct oral administration, the dried granules are milled again to a #20 sieve and dry-blended with carrier to achieve the same homogeneity criteria described for premix manufacture.
Stabilization of a preserved oral liquid containing the API begins with high-shear hydration in purified water at 60 °C for 30 min, followed by cooling to 25 °C before the addition of preservative. The liquid vehicle contains sucrose at 20–30% w/v, sorbitol at 5–10% w/v, sodium benzoate at 0.1%, and citric acid to adjust pH to 4.5–5.5. Xanthan gum is incorporated at 0.1–0.3% w/v to maintain the suspension; without this suspending agent, the botanical extract deposits within 24 h and forms a hard sediment that cannot be redistributed by patient-side shaking. The batch is homogenized at 3000 rpm for 10 min in a high-shear rotor-stator mixer, then filled into 100 mL or 250 mL high-density polyethylene bottles with polypropylene child-resistant closures. The terminal product is an oral solution or suspension for veterinary use, filled under nitrogen headspace to reduce oxidative darkening of phenolic components.
Preserved oral liquids are tested for antimicrobial effectiveness by USP <51>, and the preservative level is adjusted if challenge testing against Candida albicans and Aspergillus brasiliensis fails the acceptance criteria. The formulation is incompatible with uncoated aluminium cap liners because residual organic acids migrate into the headspace and corrode the metal; polyethylene terephthalate-coated liners are specified instead. If the product is distributed as a preservative-free single-dose oral solution, the liquid must be sterile-filtered through a 0.22 µm membrane and filled aseptically. The lower pH boundary is set at 4.0; below this point, acid-catalyzed cleavage of glycosidic bonds in the decoction extract reduces paeoniflorin assay and generates glucose, which itself becomes a fermentation substrate in contaminated non-sterile liquids.
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Siwu Decoction Powder Veterinary Grade API is supplied under three particle-size models: SWD-VG-API-F20, SWD-VG-API-F80, and SWD-VG-API-F150. The model suffix corresponds to the laser diffraction D90 specification: ≤20 µm for injectable-grade powder, ≤80 µm for tablets, capsules, and oral solutions, and ≤150 µm for powders, granules, and premix formulations. The material is an aqueous decoction extract of Rehmannia glutinosa prepared root, Paeonia lactiflora root, Angelica sinensis root, and Ligusticum chuanxiong rhizome, concentrated and spray-dried with a starch or maltodextrin carrier. Lot release includes high-performance liquid chromatography fingerprint against paeoniflorin and ferulic acid reference standards, with diode-array detection at 230 nm and 320 nm. Specifications align with the current Chinese Veterinary Pharmacopoeia for veterinary decoction powder where applicable; residual solvent levels are assessed under VICH GL18. Non-injectable models are considered non-sterile starting materials for further pharmaceutical processing and are not terminally sterilized.
The F20 model is processed by ethanol precipitation of the concentrated decoction, centrifugation at 10,000 × g, and spray drying with mannitol carrier. Particle size distribution is measured by laser diffraction per ISO 13320:2020; typical release limits are D10 ≤5 µm, D50 ≤10 µm, and D90 ≤20 µm. Bacterial endotoxin limit is ≤0.5 EU/mg by Ph. Eur. 2.6.14; the non-sterile F80 and F150 models are not controlled to this limit and must not be substituted in parenteral manufacture. Sterility for F20 is confirmed by membrane filtration per Ph. Eur. 2.6.1 after aseptic drying, but reconstituted aqueous solutions require subsequent clarification through 0.45 µm and 0.22 µm polyvinylidene fluoride membranes before filling.
Subvisible particulate matter in injectable solutions prepared from F20 is controlled by light obscuration per Ph. Eur. 2.9.19. If the decoction extract is not ethanol-precipitated, residual polysaccharides and tannins increase turbidity after 24 h at 2–8°C. Injectable process development should therefore use only F20 and perform endotoxin loading tests on the diluted bulk solution before terminal sterilisation. Strongly acidic media below pH 3.0 are incompatible due to precipitation of paeoniflorin hydrolysis products; for injectable solutions, pH is maintained at 6.0–7.0 with phosphate buffer. Endotoxin removal from plant extract is limited by the native lipopolysaccharide load of rhizome material. The ethanol precipitation step removes polysaccharides but not all endotoxin; therefore incoming root material is specified with total aerobic microbial count ≤1000 CFU/g before decoction. Depyrogenation of final containers by dry heat at 250°C for 30 min is required for parenteral packaging.
Equilibrium moisture sorption behaviour of the spray-dried extract shows water uptake of 3.2% at 40% RH, 8.5% at 60% RH, and 14.8% at 75% RH at 25°C. Because the starch carrier loses free-flow properties above 6% moisture, exposure to ambient air above 60% RH for more than 30 min is not recommended. Before dry granulation or tableting, the material is pre-dried in a fluid-bed dryer with inlet air at 55–65°C until loss on drying is ≤3.0% by USP <731>.
Roller compaction is preferred over aqueous wet granulation because starch-bound extracts hydrate rapidly and can form paste on impeller surfaces. In a Freund-Vector TFC-Labo roller compactor, roll force of 7–9 kN/cm, roller gap 1.5–2.0 mm, and screen size 0.8 mm produce granules with bulk density 0.48–0.55 g/cm³ and Carr index 18–22. If aqueous granulation is unavoidable, the binder solution should be limited to 10–15% w/w of dry mass and added at a rate of 0.5–1.0 kg/min per 10 kg charge to avoid overwetting. High-shear granulators with impeller tip speeds below 8 m/s produce non-uniform granules because hydrophobic cuticle fragments from Paeonia lactiflora root are not fully dispersed. Residual moisture after drying should not fall below 2.0% because electrostatic charge increases and powder clings to stainless steel surfaces.
Tablet and capsule processing of the F80 model requires attention to segregation during direct compression. A preblend of 20% w/w API, 70% microcrystalline cellulose PH-102, 8% croscarmellose sodium, and 2% magnesium stearate is mixed in a V-blender at 25 rpm for 18 min. Lubrication is performed separately for 3 min with magnesium stearate to avoid over-lubrication. Rotary tablet presses operating at 60,000 tablets/h produce tablets with friability ≤1.0% by Ph. Eur. 2.9.7 and disintegration ≤15 min in 0.1 M HCl by Ph. Eur. 2.9.1. Capsule filling uses F80 blended with lactose monohydrate; tamping pins are set to achieve slug density 0.55–0.65 g/cm³. For powders and granules, the F150 model is diluted with corn starch or glucose in a ribbon blender. Homogeneity relative standard deviation is ≤5.0% at 2% w/w API after 15 min blending at 20 rpm. For premix, the powder is dispersed onto feed carriers at 0.5–1.0 kg/tonne final feed; dusting potential is controlled by adding 1–2% vegetable oil after blending. For oral solutions, the F80 or F150 model is dissolved in purified water at 45–55°C under stirring for 30 min. Residual insoluble material is removed through a 10 µm polypropylene filter; filtrate pH is adjusted to 6.0–7.5 before filling.
Veterinary-grade acceptance requires lower microbial and elemental burdens than food-grade botanical powders. The matrix in Table 1 defines release limits for all models; injectable F20 has additional endotoxin and sterility requirements.
| Parameter | Method | Release Limit |
|---|---|---|
| Identification of paeoniflorin and ferulic acid | HPTLC / HPLC | Peaks correspond to reference |
| Loss on drying | USP <731> / Ph. Eur. 2.2.32 | ≤5.0% |
| Total ash | Ph. Eur. 2.4.16 | ≤8.0% |
| Acid-insoluble ash | Ph. Eur. 2.4.16 | ≤2.0% |
| Lead | USP <233> / ICP-MS | ≤5 mg/kg |
| Cadmium | USP <233> / ICP-MS | ≤0.5 mg/kg |
| Arsenic | USP <233> / ICP-MS | ≤2 mg/kg |
| Mercury | USP <233> / ICP-MS | ≤0.3 mg/kg |
| Aflatoxin B1 | LC-MS/MS | ≤5 µg/kg |
| Total aflatoxin | LC-MS/MS | ≤10 µg/kg |
| Total aerobic microbial count | USP <61> | ≤1000 CFU/g |
| Total yeast and mold count | USP <61> | ≤100 CFU/g |
| Escherichia coli | USP <62> | Absent/g |
| Salmonella | USP <62> | Absent/25 g |
| Bacterial endotoxin, F20 only | Ph. Eur. 2.6.14 | ≤0.5 EU/mg |
| Residual ethanol | GC headspace | ≤0.05% w/w |
| Particle size D90 | ISO 13320:2020 | Model-specific |
The powder form reduces alcohol load and transport mass compared with fluid extracts, but it introduces dispersion challenges in cold water. At water temperatures below 12°C, complete dispersion of F150 can exceed 90 min; pre-wetting with a 1:1 ethanol-water mixture before addition to the medicated water tank shortens this to 15–20 min. Viscosity of a 10% w/w dispersion at 20°C is 18–25 mPa·s when measured by Brookfield viscometer at 60 rpm; this is low enough for proportioner pumps but may cause settling in standing tanks without recirculation.
Compared with ungraded herbal powder, the veterinary-grade API is controlled for particle size, heavy metals, aflatoxins, and microbial limits. This reduces batch-to-batch variation in premix homogeneity and permits use in facilities certified under current good manufacturing practice for veterinary medicinal products. Compared with single-herb APIs such as isolated paeoniflorin or ferulic acid, Siwu Decoction Powder retains co-extracted polysaccharides, tannins, and organic acids; these components alter dissolution profiles and may interact with metal ions in hard water. Hard water with calcium carbonate equivalent above 300 mg/L can precipitate tannin-calcium complexes; chelation with disodium EDTA at 0.05–0.1% w/w is required in such water.
Comparative data relevant to manufacturer selection are summarised in Table 2. The values represent typical release specifications, not field efficacy data.
| Attribute | Siwu Decoction Powder veterinary API | Fluid extract | Ungraded herbal powder | Single-marker API |
|---|---|---|---|---|
| Particle size control | D90 ≤20/80/150 µm by ISO 13320:2020 | Not applicable; liquid | Not controlled | Controlled by crystallisation or synthesis |
| Microbial limit | TAMC ≤1000 CFU/g, TYMC ≤100 CFU/g by USP <61> | Often higher; preservative-dependent | Variable | Very low or sterile |
| Marker standardisation | HPLC fingerprint of paeoniflorin and ferulic acid | Content per mL | Unstandardised | Single compound purity ≥98% |
| Residual solvent | Ethanol ≤0.05% w/w | High ethanol content | None controlled | Controlled per ICH Q3C |
| Solid dosage processing | Direct compression possible after pre-drying | Requires drying step | Poor flow and high microbial load | Compressible with excipients |
| Cold water dispersibility | 30–90 min depending on temperature | Miscible | Poor | Variable |
Compression of the F20 model into tablet formulations is not recommended because its mannitol carrier increases tablet friability at compression forces above 12 kN; F20 should be reserved for injectable or oral solution processes. The F150 model is not suitable for direct injection or capsule filling without prior milling because the larger particle fraction can cause content uniformity drift exceeding 5.0% RSD in low-dose capsules below 100 mg fill weight.