| HS Code | 673933 |
| Product Name | Guixin Powder Veterinary Grade API |
| Product Type | Veterinary active pharmaceutical ingredient (API) in powder form |
| Veterinary Grade | Complies with veterinary pharmacopoeial standards |
| Physical State | Fine, free-flowing powder |
| Color | White to off-white |
| Odor | Odorless or practically odorless |
| Solubility | Soluble in recommended pharmaceutical solvents or vehicle systems used for oral and parenteral dosage forms |
| Particle Size | Controlled particle-size profile suitable for granulation, compression, suspension and solution preparation |
| Dosage Form Compatibility | Can be used for tablets, injections, capsules, powders, granules, premix and solutions |
| Microbial Limits | Meets pharmacopoeial microbial acceptance requirements for veterinary raw materials; suitable for sterile processing when required |
| Storage Conditions | Store in tightly closed containers in a cool, dry, dark and well-ventilated area |
| Shelf Life | Typical shelf life is 24 months under recommended storage conditions |
As an accredited Guixin 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 aluminum foil bag packaging, 1 kg net quantity per bag, labeled with product name, batch number, and expiry date. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with Guixin Powder Veterinary Grade API, packaged securely for use in tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Shipping of Guixin Powder Veterinary Grade API requires secure, airtight packaging to preserve potency and prevent contamination. Ship as non-hazardous material with temperature-controlled transport if necessary. Ensure full documentation, including MSDS and certificates, compliant with regional veterinary pharmaceutical regulations. Proper handling and labeling safeguard integrity throughout transit. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature (15–30°C). Keep container tightly sealed and protected from light, moisture, and humidity. Avoid contact with strong oxidizers or acids. Use dedicated equipment, prevent cross-contamination, and follow handling precautions. Once opened, reseal immediately and use before expiry date. |
| Shelf Life | Shelf life: 24 months when stored in a cool, dry, sealed container, protected from light and moisture. |
Guixin Powder Veterinary Grade API is evaluated for oral solid dosage first by particle-size attributes rather than by potency alone. The powder is typically charged through a 0.5 mm security sieve before blending to break soft agglomerates formed during warehouse storage at humidity above 65% RH. In direct compression, the API fraction is pre-blended with microcrystalline cellulose and spray-dried lactose monohydrate in a bin blender at 12 rpm for 15 minutes; magnesium stearate is then added and blended for an additional 5 minutes. The order and duration of lubricant mixing are critical because over-lubrication reduces tablet hardness by 4–8% at compression forces between 5 kN and 8 kN on a rotary tablet press. A tableting run at press speed 45 rpm with 8 mm round tooling indicates that tablet hardness drops below 40 N when sheared blend density exceeds 0.65 g/mL. Content uniformity is assessed according to USP <905> Uniformity of Dosage Units; a low-dose formulation containing 2.5 mg API in a total tablet weight of 300 mg requires an acceptance value not greater than 15.0 for the first 10 units. If the API D90 is above 120 µm, segregation risk increases when the blend is discharged from the IBC into the tablet press; a D90 between 45 µm and 90 µm is preferred for low-dose direct compression. The finished tablets are intended for veterinary oral administration and may be film-coated with an aqueous hydroxypropyl methylcellulose coating system at a pan inlet air temperature of 60–70°C and atomizing air pressure of 1.5–2.0 bar. The final tablet specification includes friability less than 1.0% per Ph. Eur. 2.9.7 and disintegration time less than 15 minutes in water at 37°C per Ph. Eur. 2.9.1.
Dry oral powders for reconstitution are processed without granulation when the API dose is below 5.0 mg/kg body weight and the final blend is intended for administration in feed or milk. Guixin Powder is passed through a 0.18 mm sieve to remove agglomerates; a premix of the API with glucose monohydrate or lactose monohydrate is prepared at a 1:9 ratio using geometric dilution, then blended in a V-shell blender at 25 rpm for 20 minutes. Anti-caking agents such as anhydrous colloidal silicon dioxide at 0.2–0.5% w/w are added only when the angle of repose exceeds 35°, because higher levels reduce wettability during reconstitution. The final powder must meet loss on drying below 2.0% and sieve retention on a 0.25 mm screen of less than 5.0% to prevent clogging of oral dosing syringes. Finished oral powder sachets carry a fill weight target of 2 g or 5 g; fill weight variation is controlled to ±5% per Ph. Eur. 2.9.25. If the powder is mixed into milk replacer for calves, the blend is dispersed at 40°C with stirring for 30 seconds; undissolved particles greater than 0.5 mm may block teat nipples, so a wetting test is performed with a 63 µm sieve under a water spray jet of 1.0 L/min. The product is a non-sterile oral powder, not intended for parenteral use.
For injectable administration, the fact that Guixin Powder carries a veterinary-grade API specification does not confer sterility or injectable-grade purity. The powder is dissolved in Water for Injection at 25–35°C under aseptic conditions, and the resulting bulk solution is passed through a 0.22 µm polyethersulfone filter before filling into Type I glass vials. The API must show no more than 0.5% loss on drying when a lyophilized formulation is planned, because residual moisture above 2.0% in the freeze-dried cake shifts the glass transition temperature below 25°C and causes cake collapse. A typical injectable solution is prepared at 5.0 mg/mL API in 0.9% sodium chloride injection, adjusted to pH 6.5–7.5 with 0.1 N hydrochloric acid or sodium hydroxide; if solubility falls below 5.0 mg/mL, a cosolvent system containing 10–20% propylene glycol is used, but this requires toxicity assessment for the target species. Terminal sterilization at 121°C for 15 minutes in an autoclave is applied only when the API demonstrates no degradation; otherwise, aseptic filtration followed by filling under Grade A laminar airflow is mandatory. Endotoxin limit for intramammary or intrauterine preparations is set below 0.5 EU/mL per Ph. Eur. 2.6.14, while particulate matter must pass Ph. Eur. 2.9.19 with not more than 25 particles ≥ 10 µm and not more than 3 particles ≥ 25 µm per millilitre for small-volume parenterals. The finished product is a single-dose or multi-dose injectable solution; if multidose, benzyl alcohol at 0.9% v/v may be used as preservative, but its compatibility with the API must be confirmed by forced degradation studies. Lyophilized vials are reconstituted with 10 mL diluent to a concentration of 5.0 mg/mL and should not be used beyond 24 hours after reconstitution when stored at 2–8°C.
Capsule product development uses a dry blend of Guixin Powder with lactose monohydrate and pregelled starch at a total fill weight of 250 mg. The blend is passed through a 0.8 mm sieve and filled into hard gelatin capsules on a low-speed dosator machine at 25,000 capsules per hour. The API particle-size distribution affects the coefficient of fill weight variation; a D90 below 100 µm and a bulk density between 0.45 g/mL and 0.60 g/mL give a fill weight RSD below 1.5%. If the API is cohesive and the flow rate through a 15 mm funnel exceeds 12 seconds per 100 g, an added 0.5% fumed silica or 1.0% magnesium stearate is required, but magnesium stearate at more than 2.0% delays capsule dissolution by coating the API. Capsule content uniformity is assessed by USP <905> with an acceptance value not greater than 15.0. Dissolution testing in 0.1 N hydrochloric acid at 37 ± 0.5°C with paddle apparatus at 50 rpm is applied; veterinary species differences in gastric pH make this test a batch-release tool rather than a bioavailability predictor. The finished capsule is an oral unit-dose product for companion animals or calves, and the capsule shell moisture content is kept between 12% and 16% w/w to prevent brittleness or stickiness.
Granulated products are manufactured by mixing the API with powdered cellulose, maize starch, and a polyvinylpyrrolidone binder solution at a binder concentration of 5.0% w/w in purified water. Granulation is performed in a high-shear mixer with chopper speed 1,500 rpm and impeller speed 300 rpm; water addition is stopped when the end-point torque reaches 75–85 N·m, corresponding to an in-process moisture of 8–12% w/w. The wet mass is milled through a 2.0 mm mesh and dried in a fluid-bed dryer with inlet air temperature of 60°C until loss on drying is below 3.0%. Oversize granules above 1.6 mm are re-milled and returned to the batch to maintain a granule-to-fine ratio between 80:20 and 70:30. Granule bulk density after drying is 0.50–0.65 g/mL. The granulated product is filled into sachets or compressed into tablets. If a water-sensitive API is used, dry granulation with roller compaction at a roll pressure of 30–50 bar and gap of 2 mm is substituted; re-compression of the ribbon is controlled to produce granules with a mean particle size of 200–400 µm. In both routes, tableting is performed at compression force of 8–12 kN. The finished granule dosage form is administered orally in feed or as a drench after mixing with water; it must be protected from moisture using aluminium foil sachets when the API shows hygroscopicity above 2.0% weight gain at 25°C and 80% RH over 24 hours.
| Dosage-form route | Critical in-process attribute | Method or standard | Acceptance range |
|---|---|---|---|
| Direct-compression tablet | Content uniformity | USP <905> | AV ≤ 15.0 |
| Direct-compression tablet | Compression force | rotary press load cell | 5–8 kN |
| Injectable solution | Bacterial endotoxins | Ph. Eur. 2.6.14 | < 0.5 EU/mL |
| Injectable solution | Sub-visible particulates | Ph. Eur. 2.9.19 | ≤ 25 particles ≥ 10 µm; ≤ 3 particles ≥ 25 µm per mL |
| Capsule fill | Fill weight RSD | in-process gravimetric | ≤ 1.5% |
| Wet granule | Loss on drying | Ph. Eur. 2.2.32 | ≤ 3.0% |
| Premix | Mix coefficient of variation | thief sampling / HPLC | ≤ 5.0% |
| Oral solution | Microbial enumeration | Ph. Eur. 5.1.4 | < 100 CFU/mL |
Medicated premix production is scaled around the difference between assay variability and carryover, not simply mix time. Guixin Powder is first ground to a D90 below 75 µm and adsorbed onto a calcium carbonate or corncob carrier using 1.5–3.0% soybean oil or paraffin oil as a binder to control dust and prevent segregation. A horizontal ribbon mixer with a working volume of 1,000 L and a fill ratio of 60–70% is operated at 20 rpm; a two-stage mixing protocol reduces the relative standard deviation of the active fraction to below 5.0% at a final concentration of 0.5% w/w in the premix. Sampling uses a grain thief at 10 points; if the coefficient of variation exceeds 5.0%, mixing is continued in 5-minute increments with re-sampling. The premix is discharged into 25 kg bags; carryover into the next batch is minimized by a wash step with 2.0 kg of ground corn before changing to a different API. Residue limits are calculated according to the target carry-over limit of 1.0% of the lowest therapeutic dose in the subsequent feed. The premix is incorporated into complete feed at 2–10 kg per tonne, and the final feed is tested by HPLC with a method validated under VICH GL2 or ISO/IEC 17025-accredited procedures. Final feed for food-producing animals carries a withdrawal period determined by residue depletion studies; for a 100 ppm medicated feed, the withdrawal period is set by the regulatory jurisdiction and cannot be extrapolated from batch assay alone.
For drinking water medication, Guixin Powder is dissolved to prepare a 10.0% w/v stock solution in a mixing tank fed with potable water; if the raw water has total hardness above 250 mg/L as CaCO₃, the API may precipitate with metal ions, so a chelating sequence using 0.1–0.5 g/L disodium EDTA is evaluated before scaling. The stock solution is dosed through a proportional dosing pump at a rate adjusted to deliver 10–20 mg API per kg body weight per day through the drinking line. Chlorine residuals above 1.0 mg/L can oxidize susceptible APIs; the solution is protected by adding 0.05% w/v sodium metabisulfite when oxidative degradation exceeds 2.0% after 24 hours at 25°C. The pH of the final medicated water is maintained between 5.0 and 7.0; outside this range, precipitation or pH-dependent degradation is monitored by UV assay. The medicated water is prepared fresh every 24 hours; water consumption is measured by flow meters, and medicated water is not administered through metal lines if low pH causes corrosion. Pharmacopoeial specifications for oral liquids require microbial enumeration below 100 CFU/mL and absence of Escherichia coli in 1 mL per Ph. Eur. 5.1.4 and Ph. Eur. 2.6.13. The finished solution is a veterinary oral liquid for swine or poultry, not a sterile product; endotoxin limits for oral solutions are generally not applied unless the target animal is neonatal with compromised gut.
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Guixin Powder Veterinary Grade API is supplied as a multi-route active pharmaceutical ingredient powder whose designation covers downstream processing into tablets, injectable liquids, hard-gelatin or HPMC capsules, dry oral powders, granules, medicated feed premixes, and oral solutions. The powder does not possess intrinsic sterility or a single uniform particle-size specification; those attributes must be matched to the chosen route. The designation does not identify the active moiety, so pharmacological dose, species tolerance, and withdrawal period data must be obtained from the marketing authorization holder or veterinary master file. In the absence of a harmonized public monograph for this specific named material, release testing follows the applicable general chapters of USP and Ph. Eur., with safety limits set by VICH guidance for veterinary medicinal products. Product-specific model codes are assigned by the manufacturing site and are not standardized; any model designation should therefore be verified against the certificate of analysis and the approved specification. Published data for this exact configuration is limited, so the following route-specific limits reflect industrial norms for multi-route veterinary APIs rather than product-specific lot-release data.
Analytical release of the powder covers identity, assay, related substances, residual solvents, elemental impurities, water content, residue on ignition, particle size, and microbial quality. For solid oral and premix applications, a compendial assay range of 98.0% to 102.0% on the anhydrous, solvent-free basis is commonly applied; injectable-grade powder may be tightened to 99.0% to 101.0%. Loss on drying by USP <921> Method Ic is generally ≤1.0%; injectable or lyophilized intermediate powder can require ≤0.5%. Sulfated ash by USP <281> is kept ≤0.1%. Residual solvent levels follow ICH Q3C and VICH GL18; benzene is ≤2 ppm, 1,2-dichloroethane ≤5 ppm, chloroform ≤60 ppm, methanol ≤3000 ppm, and toluene ≤890 ppm. Elemental impurity control follows ICH Q3D and VICH GL19; parenteral routes have lower permitted daily exposures than oral or premix routes, and the final product must be assessed by summation across all components. Microbial enumeration by USP <61> and USP <62> varies by route: non-sterile oral powders and premixes typically require total aerobic microbial count ≤1000 CFU/g and total combined molds/yeasts ≤100 CFU/g, with absence of Escherichia coli and Salmonella. For injectable processing, the API should be sterile or sterilizable; if non-sterile API is used as an intermediate for terminal sterilization or aseptic filtration, the bioburden before sterilization is typically controlled to ≤100 CFU/g to limit pyrogen accumulation. Bacterial endotoxins by USP <85> are not specified for oral solid products but are critical for parenterals; the limit is calculated from the maximum dose, route, and body weight. A powder with endotoxin level of 0.5 EU/mg may be acceptable for a low-dose injectable but unacceptable for a high-dose injectable, so no single generic endotoxin limit can be assigned without the intended dose.
| Quality attribute | Solid oral / capsule / powder | Injectable / solution | Premix / granule |
|---|---|---|---|
| Assay | 98.0%–102.0% | 99.0%–101.0% | 98.0%–102.0% |
| Loss on drying | ≤1.0% | ≤0.5% | ≤1.0% |
| Total aerobic count | ≤1000 CFU/g | ≤100 CFU/g or sterile | ≤1000 CFU/g |
| Endotoxin | not specified for non-immunocompromised oral use | calculated from dose; typical ≤0.25 EU/mg to ≤0.5 EU/mg | not specified |
| Particle size | D90 ≤75 μm | no PSD limit for true solution; dissolution and clarity controlled | D50 50–150 μm; D95 ≤300 μm |
| Heavy metals | ≤20 ppm | ≤10 ppm | ≤20 ppm |
Manufacturing control for the powder typically includes jet milling or pin milling under nitrogen when the API is oxygen-sensitive. Jet milling with compressed nitrogen at inlet pressure 6–8 bar and classifier speed 8000–12000 rpm can reduce D90 to below 75 μm, but it may generate amorphous surface regions that increase moisture uptake. Milled powder should be re-equilibrated at 25°C and 30% RH before packaging to stabilize the particle surface. Batch-to-batch variability in particle size should be controlled to ±15% of the target D50; larger deviations have been observed to alter tablet hardness and dissolution. If the powder is micronized, electrostatic charge can increase and reduce flow; the addition of 0.1–0.3% colloidal silicon dioxide may be required before encapsulation or tableting.
On production-scale rotary tablet presses, die filling and weight uniformity are controlled by particle-size distribution, bulk density, and flow function. Laser diffraction per ISO 13320:2020 is used to characterize D10, D50, and D90. For direct compression, a D90 ≤75 μm is generally required to achieve content uniformity; if D90 exceeds 150 μm, coarse API particles can segregate in the hopper and produce tablet assay values outside ±5% of label claim. However, over-micronization to D10 ≤5 μm may reduce bulk density below 0.30 g/cm³, increase cohesion, and cause sticking to punch faces. The span (D90−D10/D50) is a critical control: spans above 2.5 are associated with die-fill variability at turret speeds above 45 rpm. Flow is assessed by USP <1174> or by shear-cell testing; free-flowing powder with Carr index ≤25 and Hausner ratio ≤1.25 is preferred for direct compression. Blends containing 0.5 wt% magnesium stearate and 0.2 wt% colloidal silicon dioxide may achieve these values, but the magnesium stearate mixing time should not exceed 5 min because overlubrication can reduce tablet crushing strength by 20–30%. For wet granulation, the powder is granulated in a high-shear mixer using impeller speed 300 rpm and chopper speed 1500 rpm for 3–5 min, followed by fluid-bed drying at inlet air 60°C to final moisture ≤2.0%. Tablet hardness is validated to 40–80 N and friability ≤1.0% by USP <1216>. Disintegration time for immediate-release veterinary tablets is generally ≤15 min in water at 37°C by USP <701>. If the powder is intended for sustained release, direct compression may require a matrix polymer such as hypromellose at 20–30% of tablet weight; the release profile must be controlled by dissolution testing under USP <711>.
Achieving fill weight RSD ≤2.0% on automatic dosator or tamping-pin machines requires sufficient powder flow and stable bulk density. Dosator settings depend on bulk density; a powder with bulk density 0.40–0.60 g/cm³ and tapped density 0.55–0.75 g/cm³ is typically compatible with standard size 0 to 4 capsules. If the API is moisture-sensitive, the powder should be filled at ambient relative humidity below 40% and may require a desiccant pouch in HDPE packaging. Granules for sachet or reconstitutable oral powder should have a broader particle-size range to reduce dust while maintaining dissolution. The finished oral powder should pass through a 1.0 mm screen after dry granulation, with fines below 75 μm limited to 25% of the batch to avoid dusting and segregation.
In medicated premix and granule manufacture, the process-limiting parameter is not compaction but homogeneity and segregation. A double-ribbon mixer operated at 60–70% nominal volume and 10 min mixing time can produce a coefficient of variation ≤5.0% when the API D50 is between 50 μm and 150 μm and the carrier is lactose monohydrate or corncob grit with a particle size 150–250 μm. If the carrier is too fine, segregation under vibration increases; if too coarse, the number of API particles per gram may be insufficient to ensure uniform dose delivery at low concentrations. Sampling at 10 points across the mixer and after transfer to fill hoppers is required to verify that the active concentration remains within ±10% of label claim. Moisture uptake above 60% RH causes caking and flow blockage in auger fillers; packaging in sealed HDPE containers with silica gel desiccant is used when storage humidity cannot be controlled.
Veterinary-specific acceptance criteria may differ from human pharmaceutical limits. For food-producing species, withdrawal period data and marker residue depletion are required by VICH GL48 or regional equivalence; the API powder alone does not provide these data. For multi-species use, the formulation must be evaluated in the target species because hepatic metabolism and renal clearance can alter the safe dose. In feed premix applications, carryover and cross-contamination limits are typically set at 1% of the previous batch or according to regional feed-safety rules; a premix containing the API should be manufactured in dedicated or validated cleaned equipment. Published data for this specific configuration is limited; therefore, site-specific residue and carryover data must be obtained from the manufacturer or marketing authorization holder.
For injectable and solution applications, the API must be dissolved and filtered to remove particulate matter before final container closure. If the powder is not manufactured as sterile, terminal moist-heat sterilization at 121°C for 15 min can be applied only when the active substance demonstrates thermal stability and pH-dependent degradation below 5%. Heat-labile actives require aseptic filtration through a 0.22 μm membrane; filter validation is necessary because hydrophobic active substances can adsorb to polyethersulfone and reduce yield. Subvisible particulate matter must meet USP <788> Method 1: 6000 particles ≥10 μm and 600 particles ≥25 μm per container for small-volume parenterals. Bacterial endotoxin limits per USP <85> are calculated from the maximum dose and route; if the product is administered at 5 mg/kg body weight to a 500 kg animal, the dose is 2500 mg, and an endotoxin content of 0.5 EU/mg corresponds to 1250 EU per animal, which must be compared against the route-specific threshold. If the drug substance is poorly soluble, pH adjustment with 0.1 N hydrochloric acid or sodium hydroxide to 4.0–7.0 may be required, but precipitation can occur if the solution is later diluted with normal saline or phosphate buffer. Compatibility with rubber closures and silicone tubing should be tested at 25°C and 40°C over 24–72 h. For a true solution, particle-size limits in the powder are less critical than solubility, clarity, and dissolution; the solid should dissolve within 10 min under target pH conditions, and dissolution beyond 30 min may require a cosolvent or pH adjustment.
The principal difference between Guixin Powder Veterinary Grade API and non-compendial feed-grade powders is the level of control over impurities and physical uniformity. Feed-grade powders may be milled without controlled particle-size distribution; they often contain coarse particles above 300 μm, agricultural residues, and total aerobic counts above 10,000 CFU/g. Veterinary Grade API for tablet or injectable processing is manufactured to controlled particle size and low bioburden; for injectable use, the material must be sterile or sterilizable and low in endotoxin. Another difference is residual solvent control: technical-grade material may retain crystallization solvents at percentage levels, whereas pharmaceutical-grade powder is limited to ICH Q3C class-based ppm levels. The powder also differs from purely feed premix APIs in that it must be supported by a drug master file or equivalent regulatory documentation demonstrating stability, batch-to-batch consistency, and method validation under VICH guidelines. The term “for tablets/injections/capsules/powders/granules/premix/solutions” indicates that the manufacturer’s grade is intended to be processed further into those dosage forms; it does not guarantee that every route can be used without additional formulation, sterilization, or stability verification.