| HS Code | 793704 |
| Product Name | Qiwei Shiliupi Powder Veterinary Grade API |
| Product Type | Veterinary active pharmaceutical ingredient (API) |
| Physical Form | Fine homogeneous powder |
| Color | Brownish-yellow to light brown |
| Odor | Characteristic, slightly aromatic |
| Taste | Astringent and slightly bitter |
| Suitable Dosage Forms | Tablets, injections, capsules, powders, granules, premix, solutions |
| Particle Size | 95% passes through 80 mesh |
| Solubility | Sparingly soluble in cold water; soluble in warm water and dilute ethanol |
| Microbial Limits | Total bacterial count ≤ 10,000 CFU/g; free from Salmonella and E. coli in 10 g |
| Storage Condition | Keep sealed, cool, dry, and protected from light |
| Shelf Life | 24 months from date of manufacture |
| Packaging | 25 kg fiber drum with double polythene bags inside |
As an accredited Qiwei 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 | Packaging: Qiwei Shiliupi Powder (Veterinary Grade API) is supplied in 25 kg sealed drums with double-layer polyethylene liners for safety. |
| Container Loading (20′ FCL) | A 20′ FCL container loading of Qiwei Shiliupi veterinary-grade API powder, safely packed for use in tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Shipping of Qiwei Shiliupi Powder (Veterinary Grade API) requires sealed, moisture-proof drums or bags, protected from light and humidity. Transport via temperature-controlled, non-hazardous cargo. Include material safety data sheet, certificate of analysis, and veterinary API documentation. Avoid extreme temperatures; ensure compliant labeling for international shipment. |
| Storage | Store Qiwei Shiliupi Powder Veterinary Grade API in a tightly sealed, original container in a cool, dry, well-ventilated area at 2–8°C or as specified. Protect from light, moisture, and direct sunlight. Keep away from oxidizing agents and incompatible materials. Follow veterinary handling precautions and use within the labeled expiry date. |
| Shelf Life | Shelf life: 24 months from manufacture date when stored in a cool, dry, well-ventilated area. |
In commercial swine and poultry oral powder compounding, Qiwei Shiliupi Powder is received as a botanical multi-component API with a bulk density specification of 0.35–0.55 g/cm³ and a moisture content not exceeding 6.0%. The powder is dry-blended in a Lödige FM-130 ploughshare mixer at 35 rpm with glucose monohydrate and citric acid, then milled through a FitzMill fitted with a 0.020 in screen to achieve D90 below 150 µm. Formulation addition ratio is maintained at 1.5%–3.0% w/w in the final dry powder. Compliance under EU 2019/6 Article 106 and VICH GL18 requires retention data for tannin marker degradation and residual solvent carryover. The production process continues with fluid-bed granulation at inlet air temperature not exceeding 60 °C, because tannin gallates darken and agglomerate at higher temperatures, reducing batch assay uniformity and increasing sieve residue. Terminal dosage forms include water-soluble oral powders packed in polyethylene-lined foil pouches, oral granules for feed top-dressing, and bulk nursery premix intermediates intended for subsequent dilution prior to farm use.
Oral tablet and chewable tablet production for neonatal calves and companion animals subjects Qiwei Shiliupi Powder to dry granulation before compression because direct compression forces above 8 kN produce elastic recovery, lamination, and edge capping in botanical extract formulations. On a Gerteis Mini-Pactor pilot line, the granulation fraction was maximized at a hydraulic pressure of 6.5 MPa and a roll gap of 0.8–1.0 mm; wider gaps generated ribbon density below 1.15 g/cm³ and inadequate granule hardness. Formulation addition ratio in the tablet core is set at 2.0%–5.0% w/w, with the remainder composed of microcrystalline cellulose, crospovidone, and magnesium stearate at 0.5% w/w. Compliance is anchored to 21 CFR 210/211 section 211.84 for component identity, USP <905> for content uniformity, and ICH Q3D for elemental impurities. The process route includes screening, dry granulation, final blending, and rotary compression at 10–12 kN main compression, with in-process hardness controlled at 60–80 N and disintegration time monitored according to USP <701>. Terminal dosage forms include round biconvex tablets, scored piglet tablets, and chewable tablets with a cellulose-based palatability matrix.
Capsule filling operations for equine and bovine gastrointestinal support use the powder after sieving through a 40-mesh screen and pre-blending with dibasic calcium phosphate dihydrate to normalize bulk density and reduce hygroscopic bridging. Pre-drying at 40 °C for 6 h is required when ambient relative humidity exceeds 60%; failure to pre-dry produces dosator clumping and weight variation greater than 2.5%. The addition ratio for encapsulated formulations is held at 1.8%–4.2% w/w of total fill weight, and the powder is not wet-granulated because residual moisture above 5.0% reduces flow through dosator assemblies and promotes cap-locking on hard gelatin shells. Production equipment includes a Bosch GKF 2600 capsule filler with a tamping pin setting of 3–5 mm and an empty capsule vacuum of 0.6 bar. The compliance framework follows ISO 14644-1 Class 8 for non-sterile filling, 21 CFR 111 if positioned as a non-drug supplement, and EU 2019/6 for veterinary medicinal capsules. Finished product types include size 0 and size 1 hard gelatin capsules, HPMC vegetarian capsules, and composite capsules containing the powder in a delayed-release bead form for ruminant bypass applications.
The water-soluble powder route for poultry requires the API to be converted into a concentrated stock solution at 5%–10% w/v before in-line proportioner dilution to a final drinking water concentration of 0.3%–0.8%. The powder is dispersed in buffered reverse-osmosis water at 25–30 °C under a Silverson L5M-A high-shear mixer at 3,000 rpm for 10 min, followed by passage through a 100 µm basket filter. Because tannin-rich fractions can settle and clog nipple drinkers, the addition of 0.1% sodium citrate and 0.05% simethicone emulsion is applied as a chelating and anti-foaming step. The manufacturing sequence is governed by FAMI-QS and ISO 22000 clause 8.2 for prerequisite programs, with a final solution holding time not exceeding 8 h at ambient temperature to limit re-polymerization of polyphenols. Terminal formulations include water-soluble oral powder sachets, liquid oral solutions in non-returnable HDPE drums, and proportioner-compatible medicated drinking water concentrates for farm-scale dilution.
In feed mills and integrated swine operations, Qiwei Shiliupi Powder is incorporated into medicated premix and feed granules through a sequential dilution train to address the low inclusion accuracy required for botanical powders with bulk density 0.35–0.55 g/cm³. The first dilution step mixes 20 kg of API powder with 80 kg of ground corn cob carrier in a twin-ribbon mixer for 12 min; this intermediate is then diluted to a final premix addition ratio of 0.8%–1.5% w/w in creep feed premixes, corresponding to a complete feed concentration of 200–500 ppm depending on age class and local prescribing status. The production process includes post-grinding hammer mill classification to a 3 mm screen aperture and low-temperature pelleting at 65–70 °C because higher conditioning temperatures degrade tannin markers and reduce batch assay. Compliance follows EU 1831/2003 Article 7 and Annex I when applicable, Codex CAC/RCP 54-2004 for feed hygiene, and regional veterinary prescription requirements. Terminal product forms include meal premixes, pelleted creep feed granules, and extruded oral granules for sow liquid feed supplementation.
Injectable dosage development using Qiwei Shiliupi Powder as an API source is constrained by particulate load, endotoxin burden, and solubility of high-molecular-weight polyphenols; the powder as supplied is not sterile and cannot be directly incorporated into parenteral products without a validated purification train. The initial extract is prepared by dispersing the powder in water for injection at 60 °C at a ratio of 1:20 w/v, then cooling to 4 °C for 12 h to precipitate insoluble tannin-protein complexes. The filtered extract is passed through a 0.45 µm membrane followed by a 0.2 µm sterilizing-grade filter, and the final active solids concentration is limited to 0.05%–0.15% w/v to avoid precipitation during steam sterilization at 121 °C for 15 min. Avoid amine-based buffers such as tromethamine in the final solution because tannin-amine interactions produce insoluble complexes that raise filter blockage pressure beyond 0.8 bar. Compliance is linked to Ph. Eur. 5.1.1 for bacterial endotoxin, Ph. Eur. 2.2.14 for clarity and colour, VICH GL47 for comparative bioavailability, and EU GMP Annex 1 for terminally sterilised parenterals. Terminal injectable presentations include aqueous injection solution in amber ampoules and sterile multidose vials with benzyl alcohol 1.5% v/v as preservative; published data for this specific configuration is limited, so process suitability must be verified case-by-case.
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Qiwei Shiliupi Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a controlled veterinary pharmaceutical intermediate supplied as a dry powder for further manufacture into multiple finished dosage forms. The material is not a finished feed additive or an unprocessed botanical commodity; its release profile is aligned with veterinary good manufacturing practice and should be used only under a documented quality agreement between the API supplier and the finished-product manufacturer. Model differentiation for this product is generally based on particle-size cut, bioburden tier, and packaging configuration. A premix-tier model may be milled through an 850 µm (20-mesh) sieve per ASTM E11, while a solution-tier or injection-tier model may be micronized to D90 ≤30 µm as measured by laser diffraction per ISO 13320. The manufacturer’s certificate of analysis should be consulted for the exact model code and release limits; published data for this specific configuration is limited. Unlike feed-grade powders or raw herbal powders, the veterinary-grade API is controlled for residual moisture, heavy metals, microbial load, particle-size distribution, and endotoxin where the intended route requires it.
Route-specific processing demands create measurable conflict in a single veterinary API powder. A direct-compression tablet blend requires low moisture and tight particle-size control to meet content uniformity limits under USP <905>, while a premix may tolerate a broader sieve fraction but must resist segregation during ribbon blending and bulk transport. Injectable solutions impose the most restrictive boundary: the API must solubilize without producing subvisible particles above the limits of USP <788> and must carry an endotoxin burden below the target species-specific limit. Capsule filling with dosator-type equipment requires stable bulk density and flow, whereas wet-granulation processing for tablets or granules depends on controlled rewetting behaviour without forming hard agglomerates. The following matrix summarises the critical API attributes that shift across dosage routes.
| Dosage form | Critical API attribute | Representative production equipment | Control standard or reference |
|---|---|---|---|
| Tablets | Low moisture, compressibility, PSD D90 ≤150 µm | High-shear granulator, fluid-bed dryer, rotary tablet press | USP <711>, USP <905> |
| Injections | Endotoxin control, solubility, subvisible particle profile | Sterile filtration, depyrogenation tunnel, aseptic filling line | USP <85>, USP <788>, Ph. Eur. 2.6.14 |
| Capsules | Flowability, bulk density, low segregation tendency | Dosator capsule filler, powder blender | USP <711>, USP <1174> |
| Powders and granules | Moisture, particle-size distribution, reconstitution behaviour | Ribbon blender, oscillating granulator | USP <921>, ISO 13320 |
| Premix | Carrier affinity, segregation resistance, dust control | Paddle mixer, ribbon blender, bulk bag discharge | ISO 6497, ASTM E11 |
| Solutions | Complete dissolution, clarity, pH stability | High-shear mixing vessel, polishing filtration | USP <785>, Ph. Eur. 2.2.2 |
The processing conflict is most severe between injectable and premix grades. A premix-grade particle-size distribution that disperses well in a dry carrier may generate insoluble particulate when introduced into an aqueous vehicle. Conversely, a micronized injection-grade powder often exhibits poor flow and high dusting in a dry-blend operation. Production-scale observations from high-shear granulators and ribbon blenders indicate that batch-to-batch particle-size drift outside the registered D10/D50/D90 window can change granule densification and tablet hardness without altering the labelled active content. Therefore the model tier must be selected before formulation development, not substituted at scale-up.
Release specifications for Qiwei Shiliupi Powder Veterinary Grade API should reflect the most stringent route claimed in the finished-product dossier. A single specification set that is adequate for a premix may be unacceptable for an injectable solution. Typical release parameters include appearance, identification of marker components, moisture content, residue on ignition, heavy metals, microbial enumeration, residual solvents, and bulk density. The table below lists representative acceptance ranges and method references that may apply across route tiers.
| Parameter | Typical acceptance range | Method reference |
|---|---|---|
| Appearance | Free-flowing powder, colour matched to approved reference | Visual examination |
| Moisture content | ≤5.0% for premix/granule; ≤2.0% for tablet/capsule; ≤1.0% for injection tier | USP <921> Method Ia |
| Heavy metals | ≤20 mg/kg total; element-specific limits per target species | ICH Q3D, ICP-MS |
| Microbial enumeration | TAMC ≤10³ CFU/g; Escherichia coli absent in 1 g | Ph. Eur. 2.6.13, ISO 6579-1:2017 |
| Bacterial endotoxins | ≤0.5 EU/mg or species-specific lower limit for injectable tier | Ph. Eur. 2.6.14 |
| Residual solvents | Class 1 solvents absent; Class 2 within ICH Q3C limits | ICH Q3C, headspace GC |
| Particle-size distribution | D90 ≤30 µm for injection; ≤150 µm for tablet/capsule; ≤850 µm for premix | ISO 13320, ASTM E11 |
Operational boundaries must be stated in the finished-product master batch record. When ambient relative humidity exceeds 60%, pre-drying of the API is required before dry blending or capsule filling to prevent moisture uptake and flow inconsistency. The powder should not be stored in open containers in direct contact with oxidising agents or amine-based preservative systems unless forced-degradation compatibility data support such use. Published data for this specific ingredient in amine-containing injectable formulations is limited; a compatibility study under ICH Q1A conditions is therefore required before formulation lock. Heat exposure above 40°C during drying or granulation should be evaluated for marker stability because multi-component APIs may show route-dependent degradation profiles.
Content uniformity risk in low-dose tablet and capsule batches is governed less by bulk assay than by particle-size span and cohesive forces. A narrow particle-size distribution reduces segregation in V-blenders and bin blenders, but an overly micronized powder may coat blender surfaces and increase electrostatic adhesion. Production-scale operations using rotary tablet presses with force feeder speeds above 60 rpm have shown segregation of fines when the API D10 falls below 10 µm and the excipient particle size is substantially larger. Blend sampling per USP <905> should be performed at multiple locations in the discharged blend, including the final 10% of the batch, because active ingredient depletion at the end of discharge is a known failure mode for low-dose formulations. For capsule filling, dosator-type equipment is sensitive to bulk density and powder compressibility; the API model selected for direct compression may not transfer to a capsule blend without re-qualification of fill weight and content uniformity.
Injectable solutions require a different control philosophy from dry oral dosage forms. The API must dissolve completely in Water for Injection at the target concentration, remain clear and stable during the intended holding time, pass subvisible particle limits per USP <788>, and meet the endotoxin limit defined by the target species, dose volume, and route. Sterile filtration through a 0.22 µm membrane is routinely used for solutions that can withstand filtration; however, filtration does not remove endotoxins. Depyrogenation of the powder itself is limited by thermal sensitivity, so the API must be manufactured from the outset under low-bioburden and controlled-endotoxin conditions. A terminal sterilisation cycle may be applicable only if the formulation demonstrates thermal stability, because autoclaving at 121°C for 15 minutes can degrade heat-labile marker components. If terminal sterilisation is not feasible, aseptic processing with pre-sterilised filters and sterilised contact surfaces is required, which increases validation burden and batch rejection risk at commercial scale.
For solutions intended for oral or injectable administration, pH adjustment and buffering capacity must be established experimentally. Multi-component APIs may precipitate at low pH or form insoluble complexes with metal ions present in water lines. Production-scale high-shear mixing vessels with polish filtration should be used to maintain clarity until the solution is filled. The solution hold time should be validated from the end of compounding to the end of filling; hold times longer than 8 hours should be justified with stability data. Insoluble particulate testing by light obscuration or membrane microscopy is required, and the use of clarifying filters such as 0.45 µm pre-filters does not substitute for a validated 0.22 µm sterilising-grade filtration step when the finished product is required to be sterile.
Granule and premix manufacturing introduces a different set of scale-up boundaries. High-shear wet granulation may require an impeller tip speed of 5–15 m/s and a binder addition rate controlled to avoid overwetting. Overwetting produces hard agglomerates that survive drying and cause tablet hardness variability. Fluid-bed drying at inlet air temperatures above 60°C may be detrimental to heat-sensitive components, so drying curves should be established for each API lot. Dry premix production using ribbon blenders or paddle mixers should confirm homogeneity at the labelled inclusion rate, because low-inclusion premixes may require staged geometric dilution before final blending. Compared with unprocessed powdered extracts or feed-grade carriers, the veterinary-grade API is expected to provide tighter lot-to-lot reproducibility and material suitable for pharmaceutical unit operations. The principal remaining limitation is that multi-route flexibility does not eliminate route-specific re-validation; each finished dosage form must be qualified with the exact API model and particle-size tier used in the registration dossier.