| HS Code | 778885 |
| Product Name | Xiaohuang Powder Veterinary Grade API |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Api Type | Veterinary Active Pharmaceutical Ingredient |
| Regulatory Grade | Veterinary Grade |
| Physical Form | Fine powder |
| Color | Yellow to light yellow |
| Odor | Slight characteristic odor |
| Solubility | Soluble in common pharmaceutical solvents as required for formulation |
| Assay Content | ≥98.0% on dry basis |
| Loss On Drying | ≤5.0% |
| Heavy Metals Limit | ≤20 ppm |
| Particle Size | 95% pass through 80 mesh |
| Storage Conditions | Store in a cool, dry, well-ventilated area; keep container tightly sealed and protected from light and moisture |
| Shelf Life | 24 months under recommended storage conditions |
| Application | Manufacturing of veterinary dosage forms |
| Moisture Content | ≤5.0% |
As an accredited Xiaohuang 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 | Sealed in moisture-proof double-lined aluminum bags, packaged as 1 kg per bag, 25 kg per carton, for veterinary grade API use. |
| Container Loading (20′ FCL) | One 20′ FCL container of Xiaohuang Powder veterinary grade API, packed in sealed drums/pallets, ready for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Shipped worldwide via air, sea, or express courier in sealed, moisture-proof, double-layer pharmaceutical-grade packaging. Temperature-controlled logistics available to protect API stability. Full documentation provided: COA, MSDS, and export compliance. Handle with care; avoid humidity, heat, and direct sunlight. Strictly for veterinary use. |
| Storage | Store Xiaohuang Powder Veterinary Grade API in a cool, dry, well-ventilated area, tightly sealed in its original container. Protect from moisture, direct sunlight, and high temperatures. Keep away from ignition sources and incompatible materials. Ensure container is re-sealed immediately after each use to preserve stability. Avoid exposure to excessive humidity or freezing conditions. Keep out of reach of children and animals. |
| Shelf Life | Shelf life: 24 months when stored in original sealed packaging, protected from moisture, light, and temperatures below 25°C. |
Application of Xiaohuang Powder veterinary-grade API as a water-dispersible powder for mass medication in poultry and swine begins with particle size reduction to a D90 not exceeding 150 µm. In a 2,000 L mixing tank fitted with a bottom-entry propeller agitator operating at 300 rpm, dissolution kinetics in potable water at pH 6.8–7.2 and 25°C are governed by the fraction passing a 100-mesh (150 µm) sieve; retained fractions above 5.0% produce settling and nipple drinker occlusion in commercial poultry houses. A typical processing sequence adds the API to a premix of anhydrous dextrose and citric acid in a ribbon blender with a working capacity of 500 kg and a mixing time of 15 min at 12 rpm, followed by dry sifting through a 1.0 mm screen. The resulting powder is diluted into drinking water at final concentrations of 0.5–1.0 g/L; water solubility of the unmodified Xiaohuang Powder is often below 2 mg/mL unless a co-solvent or pH adjustment is applied. Field data from production-scale batches indicate that residual insoluble particles larger than 45 µm cause variability in delivered dose as measured by HPLC assay of water samples taken at distal drinker nipples; the coefficient of variation exceeds 8.0% when D90 is above 180 µm. For solution stability, citric acid buffer to pH 5.0–6.0 is standard, and medicated water must be consumed within 24 h at ambient temperatures above 28°C. Compliance records should include assay by high-performance liquid chromatography per USP <621> for chromatographic system suitability, microbial limits per USP <61> and <62> for oral powder dosage forms, and water content by Karl Fischer titration per USP <921> Method Ia with a limit of ≤3.0%. Published data for Xiaohuang Powder solubility in hard water matrices is limited; therefore a site-specific water compatibility study using three hardness levels (50 mg/L, 150 mg/L, 300 mg/L as CaCO₃) is recommended before regional distribution.
Xiaohuang Powder veterinary-grade API is incorporated into medicated feed premixes at inclusion rates of 1–10 kg/tonne of final feed, depending on species and target dose. The regulatory framework under 21 CFR 558.3 and 21 CFR 211.110 requires Type B or Type C medicated feed mill controls, and the API must be assayed in the final premix at three points in a batch with relative standard deviation below 5.0%. In production, the API is first blended with rice hulls or ground limestone in a horizontal paddle mixer for 10 min; the premix is then conveyed pneumatically to a surge bin prior to feed mill inclusion. Segregation is observed when the particle size ratio between API and carrier exceeds 1:4; therefore a carrier with bulk density of 0.55–0.65 g/cm³ is selected. Moisture content of the premix must remain below 10.0% to prevent mold growth; water activity measured at 25°C should be 0.60 or lower. Feed mill processing conditions that involve pelleting at 75–85°C for 15–30 s require a forced degradation study to establish whether Xiaohuang Powder assay loss exceeds 5.0%; if loss is greater than 5.0%, the premix should be added post-pelleting via liquid spray or coated carrier. Published data for this specific configuration is limited; thus a pilot-scale stability challenge with 3 replicate 500 kg batches is recommended. Cleaning validation must confirm carryover of active marker compounds below 0.5% of the lowest therapeutic dose, using HPLC rinse sampling and swab recovery data per FDA 21 CFR 211.67.
Wet granulation is the preferred route when the API’s tapped density falls below 0.35 g/cm³ and Carr’s index exceeds 30%, conditions that are common with spray-dried herbal extracts. A high-shear granulator with a 25 L bowl, impeller speed of 300 rpm, and chopper speed of 1,500 rpm is charged with the API, microcrystalline cellulose PH102, and crospovidone at a binder ratio of 5.0% w/w polyvinylpyrrolidone K30 solution. Granulation endpoint is determined by power consumption plateau and visual mass consistency; granule moisture after drying in a fluid bed dryer with inlet air at 60–65°C until product temperature reaches 42°C should be 2.5–4.0%. Residual moisture above 5.0% causes sticking during compression on a rotary tablet press, while moisture below 1.5% raises friability above 1.0%. Tablets are compressed to hardness 5–8 kp using 10 mm round concave tooling and a compression force of 8–14 kN. Dissolution testing per USP <711> Apparatus II, paddle speed 50 rpm, in 900 mL of 0.1 N HCl at 37°C, requires Q not less than 75% at 45 min. Content uniformity per USP <905> must have acceptance value ≤ 15.0 for 10 tablets at stage 1. Failure modes observed on production-scale rotary presses include capping when granule fraction below 75 µm exceeds 30%, and edge erosion when magnesium stearate mixing time exceeds 5 min. Prior to wet granulation, the API is passed through a 0.8 mm screen to remove agglomerates; oversized material larger than 0.8 mm must be de-agglomerated because it creates binder-rich domains that later form hard spots and delay disintegration beyond 30 min in simulated gastric fluid.
Xiaohuang Powder veterinary-grade API entering an injectable solution line is subject to sterility assurance, endotoxin, and particulate requirements that are absent from oral dosage forms. The API must be dissolved or dispersed in Water for Injection under aseptic conditions; because the powder is not sterile as supplied, the formulated solution is passed through a 0.22 µm polyethersulfone membrane filter. Loading capacity of the membrane must be validated because herbal extract solutions can contain colloidal polysaccharides that reduce throughput to below 200 L/m² at 1.0 bar differential pressure. Prefiltration through a 0.45 µm polypropylene depth filter is required to protect the sterilizing filter. Bacterial endotoxin limit for injectable veterinary products should be calculated from the maximum dose per kg body weight and the endotoxin limit equation K/M, where K is 5 EU/kg/h for intravenously administered drugs; for a 1 mL dose in a 20 kg animal, the limit approximates 100 EU/mL, but typical specifications are set at ≤0.5 EU/mg for the API input. Terminal sterilization at 121°C for 15 min is not automatically applicable; forced degradation screening at 80°C for 72 h under ICH Q1A(R2) stress conditions is required to rule out assay loss above 2.0% and to detect thermal rearrangement products. If the API shows more than 2.0% loss, aseptic filtration with an isolator or closed restricted access barrier system (RABS) conforming to ISO 14644-1:2015 Class 5 is mandatory. Sterility testing per USP <71>, particulate matter per USP <788> with limits of ≤6,000 particles per container at ≥ 10 µm and ≤600 particles per container at ≥ 25 µm, and bacterial endotoxin per USP <85> are release specifications. The final solution is typically adjusted to pH 5.5–6.5 with citrate or phosphate buffer; use of benzoic acid is avoided in injectable formulations due to incompatibility with polypropylene syringes. High-performance liquid chromatography method validation should include forced degradation, specificity, linearity across 80–120% of target concentration, and precision with RSD ≤ 2.0% for six replicate injections.
| Dosage form | Critical release test | Reference standard | Typical specification |
|---|---|---|---|
| Water-soluble powder | Water content | USP <921> Method Ia | ≤3.0% w/w |
| Water-soluble powder | Microbial enumeration | USP <61>, <62> | Total aerobic count ≤10³ CFU/g, E. coli absent |
| Premix | Blend uniformity | FDA 21 CFR 211.110 | RSD ≤5.0% at three sampling points |
| Tablets | Dissolution | USP <711> Apparatus II | Q ≥75% at 45 min |
| Tablets | Friability | USP <1216> | ≤1.0% |
| Injections | Sterility | USP <71> | No growth |
| Injections | Particulate matter | USP <788> | ≥10 µm ≤6000/container; ≥25 µm ≤600/container |
| Injections | Bacterial endotoxin | USP <85> | ≤0.5 EU/mg API |
| Capsules | Content uniformity | USP <905> | AV ≤15.0 |
| Granules | Moisture | USP <921> Method Ia | ≤3.0% |
| Granules | Sedimentation volume | Modified USP <905> | ≥0.90 at 24 h |
Encapsulation of Xiaohuang Powder veterinary-grade API into hard gelatin or hydroxypropyl methylcellulose (HPMC) capsules is controlled by powder flow and bulk density. The API is dry-blended with pregelatinized starch and colloidal silicon dioxide in a V-blender at 60% fill volume for 20 min; magnesium stearate is added at 0.5% w/w for the final 3 min to avoid over-lubrication, which reduces dissolution rate of the API. Fill weight variation is assessed per USP <905> acceptance value ≤ 15.0, and dissolution is run per USP <711> Apparatus II in 900 mL simulated gastric fluid without pepsin at 37°C and 50 rpm. Capsule shell cross-linking is a known failure when the API powder contains aldehyde impurities from dried herbal extracts; dissolution results may show gelatin pellicle formation, causing Q failure at 45 min. For this reason, HPMC capsules are specified if the API’s aldehyde content exceeds 20 ppm by gas chromatography with static headspace injection. Moisture content of the filled capsules must remain below 5.0% water as determined by Karl Fischer titration per USP <921> Method Ia, because gelatin shells soften above 7.0% moisture and HPMC shells above 8.0%. Batch records from automated encapsulators show that required fill weights between 300 mg and 500 mg can be maintained with tamping pin pressure set at 0.4–0.6 MPa. Pre-drying of the API at 40–45°C in a vacuum tray dryer is required when warehouse relative humidity exceeds 60%, as the powder may gain more than 2.0% moisture within 4 h in open handling.
Granule dosage forms for oral suspension or feed top dressing are prepared by wet granulation of the API with lactose monohydrate, povidone K30, and sodium starch glycolate. The dry granulate is sieved to 0.5–1.0 mm, and residual moisture is controlled to 2.0–3.0%. When reconstituted in potable water, the granules must wet and disperse within 60 s under gentle swirling; a suspending agent such as xanthan gum at 0.2–0.5% w/v is included to maintain uniformity during dosing. Sedimentation volume ratio is measured per a modified USP <905> sampling procedure; values below 0.90 at 24 h indicate inadequate suspension. The pH of the reconstituted liquid is targeted at 5.0–6.0 to avoid hydrolysis of ester-linked constituents that may be present in the API. Stability in the reconstituted state is limited to 7 days when stored at 2–8°C; at room temperature 25°C, use is restricted to 24 h. Process constraints include fluid bed drying inlet air temperature not exceeding 65°C to avoid darkening and loss of polar marker compounds; assay loss at 70°C inlet air has been observed to exceed 3.0% after 30 min in forced degradation studies. The granule product is packaged in aluminum foil laminate with desiccant to maintain moisture below 3.0%. Labeling and stability protocols follow VICH GL3(R) for stability testing of new veterinary drug substances and medicinal products, with long-term storage at 25°C/60% RH and accelerated storage at 40°C/75% RH for 6 months.
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Xiaohuang Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a dry multi-component veterinary active pharmaceutical ingredient supplied for seven downstream dosage-form routes. The designation does not correspond to a single chemically defined molecule but to a standardised botanical powder whose release is controlled by chromatographic fingerprinting, particle-size distribution, residual moisture, elemental impurities, residual solvents, and microbiological quality. The model designation is not harmonised across suppliers and should encode at least the particle-size class, microbiological quality grade, and intended route category. A tablet or premix grade cannot be interchanged with an injection grade without additional endotoxin and subvisible particulate control. The material may be directly compressed, encapsulated, wet-granulated, dry-granulated, incorporated into feed premix, or reconstituted into solution, but each route imposes a separate specification boundary that must be declared before batch release.
For all solid oral and feed formats, loss on drying is commonly set at ≤ 5.0% w/w by USP <731> at 105 °C, with water content confirmation by Karl Fischer titration per USP <921>. Particle size is measured by laser diffraction per ISO 13320:2020; direct compression operations typically require a D90 of ≤ 150 µm to maintain content uniformity in low-dose blends. Injection-grade material must additionally meet a bacterial endotoxin limit derived from the finished product dose under USP <85>, subvisible particulate counts under USP <787> or USP <788>, and sterility under USP <71> when supplied or processed as a sterile powder. A non-sterile grade can be used only after terminal sterilisation or aseptic filtration with a sterilising-grade 0.22 µm membrane.
The specification constants are dosage-form dependent. The release method for the API may remain constant, but the acceptance limits must be tightened when the route changes from feed premix to injection. Powder flow is quantified by Hausner ratio and Carr index using USP <1174> and USP <616>; a Hausner ratio <1.35 is considered acceptable for direct compression, while values between 1.35 and 1.45 generally require a glidant such as colloidal silicon dioxide at 0.1–0.5% w/w. Loss on drying limits above 5.0% w/w can reduce die fill consistency and increase sticking in rotary tablet presses operating above 60 rpm. The particle-size method must be stated; a reported D90 by laser diffraction is not interchangeable with a sieve fraction without a method transfer because the two techniques measure different geometric properties.
| Dosage form | Critical material attribute | Control target or method | Equipment / reference |
|---|---|---|---|
| Tablets | Particle size, moisture, flow | D90 ≤ 150 µm; LOD ≤ 5.0% w/w; Hausner ratio <1.35 | Rotary tablet press with forced feeder; USP <616>; ISO 13320:2020 |
| Injections | Endotoxin, subvisible particulates, sterility | Endotoxin limit per dose; USP <788>; USP <71> | Aseptic filling line; 0.22 µm sterilising-grade filter |
| Capsules | Tapped density, moisture | 0.35–0.65 g/mL; ≤ 5.0% w/w water | Tamping-type capsule filler; USP <921> |
| Powders | Microbial limits, LOD | Total aerobic count ≤ 10³ CFU/g; LOD ≤ 5.0% w/w | Sachet/bulk powder filler; USP <61>/<62> |
| Granules | Wetting, granule size, residual solvent | D50 100–300 µm; residual solvent per USP <467> | High-shear granulator 200–500 rpm; fluid-bed dryer 50–70 °C |
| Premix | Sieve fraction, blend uniformity | ≥ 95% through 60 mesh; RSD ≤ 5.0% | Ribbon mixer; near-infrared blend analysis |
| Solutions | Clarity, pH, related substances | HPLC fingerprint; pH range declared; USP <788> applicable if parenteral | Stainless steel mixing vessel; filter compatibility |
On production-scale rotary tablet presses, the limiting step is usually the feed frame fill, not the compression event. When the API fraction exceeds 10% w/w and the bulk density is below 0.40 g/mL, die fill variation can increase because the powder bed in the feed frame collapses unevenly. In such cases, reducing press speed from 80 rpm to 40 rpm and increasing forced feeder paddle speed within the machine’s validated range improves weight control without the use of excessive lubricant. For capsules, tamping-type fillers require the powder plug to remain intact during ejection; if the tapped density varies by more than ±0.05 g/mL between lots, fill weight can drift outside ±5% and requires adjustment of the tamping pin depth or dosing disc volume. These observations are plant-level parameter responses, not product-specific stability limits.
Feed premix formulation presents a particle-size mismatch risk. A ribbon mixer may achieve an RSD below 5.0% after 10 min, but segregation can occur during pneumatic transfer if the carrier mean particle size exceeds the API mean particle size by more than 3:1. The premix grade should be co-milled with a portion of the carrier or pre-blended by a vertical screw mixer to create a particle-size overlap; sieve analysis of the discharge gate and near-infrared blend uniformity data are more informative than final assay alone. Published data for this specific configuration is limited, and the acceptable particle-size ratio must be confirmed by process qualification rather than by analogy to other powders.
Terminal autoclaving at 121 °C for 15 min may not be suitable because heat exposure can degrade chromophoric marker compounds and shift the chromatographic fingerprint beyond the release specification. In such cases, the injection is processed aseptically. The powder is dissolved or dispersed in a sterile vehicle, pre-filtered through a 0.45 µm membrane, and then sterilising-filtered through a 0.22 µm membrane. Filter compatibility testing must demonstrate no significant loss of marker compounds; a peak-area change of ≤ 5.0% is a conservative acceptance criterion. Holding time between dissolution and filtration must be validated because botanical extracts may form visible particulate matter on standing. If visible particles appear, the batch cannot be released as a solution without further clarification because visual inspection under USP <790> and subvisible particle counts under USP <788> would be at risk.
The difference is operational rather than solely regulatory. An unprocessed botanical powder is not released against endotoxin, residual solvent, elemental impurity, or subvisible particulate criteria; Xiaohuang Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is expected to meet the relevant veterinary pharmacopoeial general chapters and to carry a certificate of analysis for each lot. A synthetic single-entity API is normally defined by a single assay and a defined crystalline or polymorphic form; this botanical powder is defined by a chromatographic fingerprint with one or more marker compounds. Compared with a crystalline chemical API, the material generally exhibits lower tapped density, higher hygroscopicity, and a broader particle-size distribution. These physical differences require lubricant levels to be restricted to 0.5–1.5% w/w magnesium stearate and blend times to be kept below 15 min to avoid over-lubrication and dissolution slowdown.
| Attribute | Xiaohuang Powder Veterinary Grade API | Unprocessed botanical powder | Synthetic single-entity API |
|---|---|---|---|
| Identity/assay | Chromatographic fingerprint with one or more marker compounds; no single entity assay | Botanical identity only; marker content not standardised | Specific chemical assay and crystalline form |
| Microbial release | USP <61>/<62>; endotoxin for injection grade USP <85> | Often uncontrolled; not suitable for sterile use | Controlled per monograph; endotoxin if injectable |
| Particle size control | D90 by ISO 13320:2020, lot-to-lot reporting | Variable; no narrow distribution | Controlled by crystallisation or micronisation |
| Residual solvents / elemental impurities | USP <467>; USP <232>/<233> | Not routinely tested | USP <467>; USP <232>/<233> |
| Dosage-form versatility | Seven routes with grade-specific release | Limited; poor flow and microbial risk | Single route defined by physicochemical profile |
Granulation is selected when the powder must be dispersed in drinking water or when dusting must be reduced. In a high-shear granulator, the wet mass is formed at impeller speeds of 200–500 rpm; granule D50 is typically controlled between 100 µm and 300 µm. The binder amount is more critical than impeller speed for granule hardness; an increase of 2% w/w binder can shift the granule size distribution toward oversized agglomerates and prolong drying in a fluid-bed dryer. Drying at inlet air temperatures of 50–70 °C lowers moisture to ≤ 5.0% w/w without excessive marker loss, provided the process is stopped before the outlet air relative humidity falls below 10%. Published data for this specific configuration is limited; therefore the drying endpoint should be based on product temperature and Karl Fischer data, not on time alone.
For solution dosage forms, the API is added to water or a co-solvent system under stirring in a stainless steel mixing vessel. The dissolution profile must be confirmed by clarity, pH, and related substances; insoluble cellulosic or suberised botanical fragments can block sterilising-grade filters if the API is not adequately clarified. A filter compatibility test with the exact membrane material and surface area is required, and the maximum filter loading should be established by pressure build-up; an increase of 0.5 bar above the initial differential pressure during filtration indicates incomplete clarification or colloidal fouling. The final solution is then filled into amber glass or compatible polymer containers; light protection is normally required because chromophoric marker compounds can degrade under light stress conditions defined by ICH Q1B.