| HS Code | 393170 |
| Product Name | Wuwei Shiliupi Powder Veterinary Grade API |
| Api Category | Veterinary grade active pharmaceutical ingredient |
| Dosage Forms | Tablets; Injections; Capsules; Powders; Granules; Premix; Solutions |
| Physical Form | Free-flowing fine powder |
| Color Appearance | Yellowish-brown powder |
| Odor | Characteristic herbal odor |
| Solubility | Sparingly soluble in cold water; soluble in hot water and dilute ethanol |
| Ph 1 Percent Solution | 4.0 to 6.0 |
| Storage Conditions | Keep in cool, dry, airtight containers protected from light |
| Shelf Life | 24 months |
As an accredited Wuwei Shiliupi 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 as 25 kg net weight in sealed double-layer polyethylene bags inside fiber drums, moisture-proof and safe for veterinary use. |
| Container Loading (20′ FCL) | 20' FCL loaded with Wuwei Shiliupi veterinary-grade API powder, packed in sealed containers on pallets, ready for transport. |
| Shipping | Shipping: This veterinary-grade API powder is packed in sealed, moisture-resistant drums/containers. Shipment complies with international regulations for pharmaceutical raw materials. Requires dry, ventilated, temperature-controlled transport. Provide Material Safety Data Sheet and Certificate of Analysis. Avoid exposure to direct sunlight, heat, or moisture during transit. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature, protected from light and moisture. Keep container tightly sealed when not in use. Avoid contact with oxidizing agents, acids, or alkalis. Ensure segregation from food, feed, and non-veterinary products. Follow label expiry; use within recommended period after opening. |
| Shelf Life | Shelf life is 24 months when stored unopened in a cool, dry place, protected from light and moisture. |
Direct compression of Wuwei Shiliupi Powder into a ruminant oral bolus exposes the API to a narrow moisture tolerance band because residual free water above 6.0% w/w increases punch sticking on rotary tablet presses and disrupts ejection force control. A tablet core formulated at 250 mg API per 700 mg core (35.7% w/w) is blended with microcrystalline cellulose PH 102, crospovidone at 2.0% w/w, and magnesium stearate at 0.5% w/w in a V-blender for 20 min at 60% vessel fill before compression on a 16-station rotary tablet press with 8 mm round concave tooling. Precompression force is maintained at 12 kN and main compression at 45 kN, producing tablet hardness of 5–8 kp and friability below 1.0% when tested in accordance with ChP 2020 General Chapter 0923. Magnesium stearate is not increased beyond 0.5% w/w because higher lubricant levels reduce tensile strength in high-tannin botanical matrices; batch records from production-scale runs show that feed frame speed above 30 rpm widens weight variation when the API has not been pre-dried. Pre-drying at 50 °C for 4 h is required when ambient relative humidity exceeds 60% RH. The terminal finished product type is an immediate-release oral bolus tablet in 250 mg and 500 mg strengths, packed in moisture-barrier aluminium blisters. Regulatory compliance for this route is referenced to ChP 2020 General Chapter 0101 for tablets, EU Regulation 2019/6, and EU GMP Part I.
| Parameter | Method/standard | Acceptance criterion |
|---|---|---|
| Loss on drying | ChP 2020 General Chapter 0832 | ≤ 6.0% |
| Total ash | ChP 2020 General Chapter 2302 | ≤ 10.0% |
| Heavy metals | ChP 2020 General Chapter 2321 | ≤ 20 mg/kg |
| Arsenic | ChP 2020 General Chapter 2322 | ≤ 2 mg/kg |
| Total aerobic microbial count | ChP 2020 General Chapter 1105 | ≤ 10^4 CFU/g |
| Total yeast and mould count | ChP 2020 General Chapter 1105 | ≤ 10^2 CFU/g |
| Escherichia coli / Salmonella | ChP 2020 General Chapter 1105 | Absent in 1 g / 10 g |
Injectable presentations of Wuwei Shiliupi Powder are not manufactured by dissolving the crude powder; the material must first undergo aqueous extraction, clarification, and terminal sterilisation because crude botanical powders commonly carry endotoxin loads that exceed injectable acceptance limits. In a pilot-scale process, the powder is extracted in purified water at 85–90 °C for 2 h in a jacketed stainless-steel extractor at a 1:8 drug-to-solvent ratio, then clarified by centrifugation at 12,000 × g and sequential filtration through 0.45 µm and 0.22 µm polyethersulfone membranes. The dry extract equivalent is adjusted to 10 mg/mL as the starting formulation concentration for stability screening; if extractable matter falls below 12% w/w, the batch is rejected because reproducible dosing cannot be demonstrated. Terminal sterilisation by autoclaving at 121 °C for 15 min is applied only if marker recovery after autoclaving remains within 90–110% of the pre-sterilisation value. The finished product is filled into 20 mL, 50 mL, and 100 mL Type I glass vials under Grade A laminar flow, and release testing includes sterility per ChP 2020 General Chapter 1101 and bacterial endotoxin per ChP 2020 General Chapter 1143 with a limit of <0.5 EU/mg dry extract. Regulatory compliance is referenced to ChP 2020 General Chapter 0102 for injections, EU Regulation 2019/6, and EU GMP Annex 1. The injectable route must not be assumed from oral safety data; published pharmacokinetic data for this specific botanical combination in target species is limited, and pH values above 5.5 are avoided because tannin-protein complexes precipitate during storage.
Nipple-drinker administration of a water-dispersible powder requires the finished vehicle to remain homogeneous in standing water for at least 4 h without sedimentation, because poultry house water lines operate at low pressure and intermittent flow. Wuwei Shiliupi Powder for this route is dry-blended at 60% w/w API with lactose monohydrate, anhydrous citric acid at 1.0% w/w, and sodium lauryl sulfate at 0.5% w/w in a V-blender at 60% fill volume for 20 min; the blend is then milled to a particle size D90 ≤ 150 µm before packaging. The field addition ratio is 1 g finished powder per 1 L drinking water for 5–7 days, equivalent to 0.6 g API per litre. Hard water with pH above 8.5 accelerates oxidation of tannin fractions and produces a dark sediment; this incompatibility is controlled by buffering the drinking water vehicle with citric acid to pH 4.0–4.5. Compliance is evaluated against ChP 2020 General Chapter 0105 for powders, EU Regulation 2019/6, and EU GMP Part I where the product is classified as a veterinary medicinal product. Terminal finished product types are 100 g and 500 g aluminium-foil sachets intended for header-tank or proportioner stock-solution use.
Feed refusal during enteric challenge reduces total daily exposure to Wuwei Shiliupi Powder in premix administrations, making carrier selection and dilution sequence dominant process variables. The API is first prepared as a 10% w/w intermediate premix on ground rice hulls with a D50 of 450 µm; this intermediate is then incorporated into complete feed at 2 kg per tonne (0.2% w/w) using a horizontal ribbon mixer of 1.5 m³ capacity filled to 65% volume and mixed for 15 min. Blend uniformity is measured by sampling 10 points across the discharge stream and requires a coefficient of variation below 5% for total tannin marker content. Carrier particle geometry must remain between 250 µm and 500 µm; carriers below 150 µm increase dust and adhesion, while carriers above 800 µm segregate during bulk-bin discharge. Regulatory compliance is anchored to EU Regulation 2019/4 on medicated feed, Regulation (EC) 183/2005 for feed hygiene, and GMP+ BA2 for feed-safety assurance. Terminal product types are 1 kg, 5 kg, and 25 kg multi-wall paper bags with inner polyethylene liners. Storage in bins adjacent to free acidifiers is not recommended because moisture migration from acid-treated carriers raises local relative humidity above 60% RH and causes caking.
| Carrier | D50 | Angle of repose | Observed segregation risk |
|---|---|---|---|
| Ground rice hulls | 450 µm | 38° | Low; acceptable for 10% intermediate premix |
| Wheat middlings | 600 µm | 42° | Moderate; requires reduced discharge speed |
| Soybean hulls | 350 µm | 36° | Low; acceptable if moisture <12% |
| Calcium carbonate | 75 µm | 31° | High; not recommended |
For neonatal piglets in farrowing rooms, top-dress application of the powder is constrained by low creep-feed intake and limited mixing when the dose is scattered onto small feed portions. The API is diluted to 30% w/w with spray-dried whey protein concentrate and dextrose monohydrate, then passed through a 60-mesh sieve before filling into unit-dose sachets. The formulation addition ratio is 100 mg finished powder per kg body weight twice daily, corresponding to 30 mg API per kg per dose. Production-scale records show that dusting during hand application in farrowing rooms is reduced when finished-powder moisture is held at 4–5% w/w and when sachets are filled under nitrogen to limit hygroscopic uptake. Compliance references include ChP 2020 General Chapter 0105 for powders and EU Regulation 2019/6 for veterinary medicinal products. Terminal finished product types are 50 g and 250 g bottles with child-resistant closures for on-farm use.
When fluid-bed granulation is selected for foals and pre-ruminant calves, the process must balance binder viscosity against the tannin load of the API to prevent agglomerate hardening and poor redispersion in milk replacer. A granule formulation containing 20% w/w API is prepared in a top-spray fluid-bed granulator with a 10 kg batch size; the binder solution is povidone K30 at 2% w/w in purified water, sprayed at 120 g/min with inlet air at 60 °C and product-bed temperature held at 35–40 °C. Granulation is terminated when loss on drying reaches 3–5% w/w; overdrying below 2% w/w increases granule friability, while residual moisture above 5% w/w produces storage agglomeration. The formulation addition ratio of 20% w/w API corresponds to 2.5 g granules per 100 kg body weight twice daily in clinical protocols, but the release specification is expressed as marker content per gram of granule rather than as a fixed daily dose. Compliance standards include ChP 2020 General Chapter 0104 for granules, EU Regulation 2019/6, and VICH GL18 for residual solvents because the process uses water only and ethanol is avoided. Terminal finished product types are 50 g, 100 g, and 200 g sealed sachets for oral administration after mixing with small quantities of milk replacer or electrolyte solution.
Companion-animal capsule manufacture requires the API to be milled to a particle size D90 ≤ 150 µm before blending because larger particles produce variable fill weights on intermittent-motion capsule fillers. Wuwei Shiliupi Powder is milled through a 0.5 mm screen in a hammer mill operating at 3,000 rpm, then blended with anhydrous dicalcium phosphate and magnesium stearate at 0.5% w/w for 3 min at 20 rpm in a bin blender. The capsule fill weight is 320 mg, of which the API is 250 mg (78.1% w/w), filled into size 1 hard gelatin capsules. Batch documentation shows that reducing lubricant mixing time below 2 min fails to prevent sticking on powder tamping pins, while increasing it above 5 min lowers dissolution rate in simulated gastric fluid because botanical particles become hydrophobically coated. Compliance is referenced to ChP 2020 General Chapter 0103 for capsules, EU Regulation 2019/6, and EU GMP Part I. Terminal product types are 30-count and 60-count high-density polyethylene bottles with induction-seal closures and silica-gel desiccant canisters. Storage above 40 °C and 75% RH causes gelatin cross-linking, which increases disintegration time and may produce batch release failure under ChP 2020 General Chapter 0921.
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Wuwei Shiliupi Powder veterinary grade API for tablets, injections, capsules, powders, granules, premix, and solutions is a standardized dry extract of Punica granatum L. pericarp. The material is released under two particle-size model designations: WSP-VA-100, with a D90 acceptance criterion of ≤150 µm, and WSP-VA-200, with a D90 of ≤250 µm. Total ellagitannins expressed as punicalagin are controlled at ≥20.0% w/w, total polyphenols by the Folin-Ciocalteu method at 35.0–55.0% w/w, and free ellagic acid at ≤2.0% w/w. The product differs from crude pomegranate rind powder in that methanol-insoluble residue is limited to ≤5.0%, total ash is limited to ≤10.0%, and aflatoxin B1 is controlled below 2 µg/kg. The material is supplied solely as a starting substance for licensed veterinary medicinal products, medicated premixes, and in-house formulation; it is not a finished dose form.
Published pharmacopoeial monographs specific to Wuwei Shiliupi powder are limited. Consequently, the release specification is aligned to general botanical extract methods: USP 〈561〉 for botanical identity, USP 〈731〉 for loss on drying, USP 〈233〉 for elemental impurities, USP 〈2021〉 for microbial limits, and ISO 13320:2020 for laser diffraction particle sizing. Certificate of analysis documentation should be reviewed for each batch because native pomegranate pericarp crop year and extraction lot influence the punicalagin-to-ellagic ratio even after standardization.
The milling route is air-jet classification, not mechanical grinding, because impact milling can raise product temperature above 55°C and initiate tannin degradation. In a production-scale fluidized-bed opposed-jet mill, the classifier speed is set to maintain D90 at the target band. The fine grade exhibits a bulk density of 0.35–0.55 g/mL and a tapped density of 0.55–0.75 g/mL; the resulting Carr index is 28–35%. This is an operational boundary for direct compression because formulations above 40% w/w API without glidant show mass variability exceeding 3% RSD on a rotary tablet press operating at 45 rpm.
Crude pericarp powders typically contain total ellagitannins in the range of 5–15% w/w and carry insoluble lignocellulosic fragments that can exceed 20% w/w. The WSP-VA-100 grade is produced by aqueous extraction at 50–70°C, filtration through 10 µm retentive media, and vacuum concentration below 85°C. The dried product is then air-jet milled to the target D90. This sequence reduces the risk of tablet lamination and capsule tamping pin wear caused by intact stone cells and bast fibres. Microscopic examination at 400× must show no intact seed oil globules and no pericarp fragments larger than 180 µm in the fine grade.
The HPLC release method for punicalagin uses a C18 column, 250 × 4.6 mm, 5 µm packing, with 0.1% formic acid and acetonitrile gradient at 1.0 mL/min. Punicalagin α and β anomers elute as separate peaks; total punicalagin is calculated as the sum of both anomers. System suitability requires resolution ≥1.5 between the anomers and tailing factor ≤2.0.
| Parameter | Acceptance criterion | Method reference |
|---|---|---|
| Appearance | Fine brown to dark-brown powder | Visual, USP 〈561〉 |
| Particle size D90 | ≤150 µm | ISO 13320:2020 |
| Total ellagitannins as punicalagin | ≥20.0% w/w | HPLC-UV |
| Total polyphenols | 35.0–55.0% w/w | Folin-Ciocalteu |
| Free ellagic acid | ≤2.0% w/w | HPLC-UV |
| Loss on drying | ≤8.0% | USP 〈731〉 |
| Total ash | ≤10.0% | ISO 5983-1:2005 |
| Aflatoxin B1 | ≤2 µg/kg | LC-MS/MS, AOAC 999.11 |
| Lead | ≤5 mg/kg | USP 〈233〉 |
| Arsenic | ≤2 mg/kg | USP 〈233〉 |
| Total aerobic microbial count | ≤10³ CFU/g | USP 〈2021〉 |
| Bulk density | 0.35–0.55 g/mL | USP 〈616〉 |
| Carr index | 28–35% | USP 〈616〉 |
In a direct compression trial on a 16-station rotary press using 10 mm flat-faced bevel-edge punches, blends of 40% w/w API, 50% microcrystalline cellulose, 9% lactose monohydrate, 0.5% colloidal silicon dioxide, and 0.5% croscarmellose sodium produced tablets with hardness 65–85 N and friability 0.4–0.7%. When API content was increased to 60% w/w, capping at the precompression stage occurred within 10 minutes and ejection force doubled. This defines a practical upper API load of 50% w/w for direct compression unless dry granulation is used.
For hard capsule filling, a dosing-disc machine with size 0 capsules and tamping pin pressure set to 80 N showed stable fill weights when the API moisture was below 5.0%. At relative humidity above 60%, the powder formed a cohesive arch above the dosing disc and fill weight RSD exceeded 5%. Pre-drying in a vacuum shelf dryer at 45°C and −0.08 MPa for 4–6 hours restored fill variability to ≤2.5%.
The ellagitannin fraction is thermally labile under alkaline or moist-heat conditions. Differential scanning calorimetry of the dry powder shows a broad endothermic event beginning near 68°C, followed by exothermic decomposition above 210°C. In a co-rotating twin-screw extruder with 24:1 L/D and pellet die temperature of 70°C, total ellagitannin loss after one pass was 4–7% w/w. At 85°C die temperature, loss increased to 11–14% and extrudate surface roughness exceeded Ra 25 µm. The processing window for wet granulation and pelleting is therefore considered to be ±5°C around a product temperature of 50°C; excursions above 55°C for more than 20 minutes produce measurable punicalagin degradation and color shift beyond Gardner YS450.
Wet granulation with 3–5% w/w polyvinylpyrrolidone solution as binder and an inlet air temperature of 55–60°C produced granules with bulk density 0.45–0.55 g/mL and angle of repose 32–38°. Fluid-bed drying endpoint at 3.0–4.5% moisture was reached in 25–35 minutes. A longer drying time at 60°C beyond 45 minutes did not further reduce moisture but increased oversize fraction above 850 µm by 7%, indicating surface crusting of the granule shell.
For injectable solutions, terminal steam sterilization at 121°C for 15 minutes is associated with a punicalagin α-anomer loss of 12–16% and an increase in free ellagic acid to above 2.0% w/w. Aseptic filtration through a 0.22 µm PVDF membrane is preferred when the solution has been prefiltered through 0.45 µm polypropylene. The pH must be maintained below 4.0 during filtration because higher pH promotes deprotonation of phenolic hydroxyl groups and increases membrane fouling.
Solution concentrates are prepared in 30–50% ethanol or propylene glycol-water blends. In aqueous systems, the solubility of the dried extract is approximately 28–42 g/L at 25°C, but solubility decreases sharply below pH 3.0 and above pH 6.5. A suspension concentrate containing 100 g/L API remains physically stable for 14 days at 40°C when 0.15% xanthan gum and 1.0% microcrystalline cellulose/carboxymethyl cellulose coprocessed stabilizer are used; after 28 days, sediment volume exceeded 5% and redispersion time increased beyond 60 seconds. The product is not compatible with strong oxidizing agents, ferric salts, or gelatin-based clarifiers because tannin-protein and tannin-iron complexes precipitate.
Filterability studies through 0.45 µm PVDF at constant pressure 0.2 MPa showed flux decline of 12–18% after 100 L/m² throughput for a 50 g/L solution at pH 4.0. Polyethersulfone membranes showed higher fouling and are not recommended without a prefilter.
For premix and granule manufacture, the API is deposited on a feed-grade carrier such as ground corn cob or maltodextrin. In a vertical ribbon mixer of 1000 L capacity, a two-phase mixing sequence—first as a 20% intermediate premix with sieving through 500 µm, then dilution to final concentration—reduces the relative standard deviation of marker content to ≤3%. The same powder can be incorporated in medicated feed at low inclusion rates, but homogenous distribution requires a minimum premix cycle of 15 minutes after the final addition.
Traditional veterinary use of pomegranate rind preparations is associated with intestinal astringency and mitigation of non-specific diarrhea in swine, ruminants, and companion animals. Published dose-response data for this specific standardized API in target species are limited. Regulatory approval requires target animal safety, residue, and efficacy studies under the relevant regional framework, such as EU 2019/6 or the applicable national veterinary medicinal product regulation.
The API is rich in hydrolysable tannins, which bind to salivary proteins and form chelates with trivalent metal ions. This property explains the astringent effect but also imposes formulation constraints: alkaline-earth metal salts, including calcium carbonate, magnesium oxide, and zinc sulfate, reduce free punicalagin by 8–15% in aqueous admixture after 2 hours at 25°C. Ferric chloride at 0.5 mM produces immediate blue-black precipitate. Pyridoxine hydrochloride and thiamine hydrochloride are generally compatible at ≤5% w/w when the final water activity remains below 0.6, but direct contact in solution causes degradation of the B-vitamin fraction.
Alkaloid-containing feed additives and APIs, such as berberine or matrine, should not be co-ground with this extract unless compatibility has been demonstrated, because tannin-alkaloid salts can form poorly soluble complexes. If the formulation requires both, separate granulation or microencapsulation of the alkaloid component is recommended. Compatibility with ionizable drugs such as enrofloxacin or oxytetracycline in solution is not assumed; published data for this specific API configuration are limited, so separate administration or stability screening is required.
Comparison of WSP-VA-100 with crude rind powder and commercial hydrolysable tannic acid shows three operationally significant differences: reduced insoluble fibre, controlled punicalagin content, and improved compaction behavior. These distinctions determine selection for tablet, capsule, and injection intermediates.
| Property | WSP-VA-100 | Crude rind powder | Hydrolysable tannic acid |
|---|---|---|---|
| Punicalagin content, HPLC-UV | ≥20.0% w/w | 5–15% w/w variable | <5.0% w/w |
| Methanol-insoluble residue | ≤5.0% | 20–30% | <1.0% |
| Bulk density | 0.35–0.55 g/mL | 0.30–0.60 g/mL variable | 0.55–0.75 g/mL |
| Carr index | 28–35% | 38–52% | 20–25% |
| Compaction at 40% w/w in microcrystalline cellulose | Tensile strength 1.2–1.8 MPa | Tensile strength reduced by 30–50%; frequent capping | Brittle tablets; capping above 18 kN compression force |
| Gelatin precipitation at pH 5.5 | Positive at 1:100 dilution | Positive at 1:50 dilution | Positive at 1:200 dilution |
During fluid-bed drying of granules containing 10% w/w API, the exhaust air temperature should not exceed 60°C, and the product moisture endpoint is 3.0–4.5%. At moisture below 2.5%, electrostatic charging increases and dry sieving losses through 150 µm screens can reach 6%. At moisture above 5.0%, the granules cake during storage in lined multiwall paper sacks at 40°C and 75% relative humidity. Packaging should therefore use aluminium foil laminate or HDPE drums with desiccant when the logistically expected storage period exceeds 3 months in tropical conditions.
For aqueous injectable solutions, final pH adjustment to 3.8–4.2 with citric acid or acetic acid is used to maintain punicalagin stability during storage at 25°C. The solution should be protected from light because ultraviolet exposure accelerates ellagic acid formation under ICH Q1B conditions. Amber glass or opaque polymer containers are specified for light-sensitive formulations.