| HS Code | 177954 |
| Product Name | Zilining Powder |
| Product Designation | Veterinary Grade API |
| Physical State | Powder |
| Api Type | Active pharmaceutical ingredient |
| Intended Dosage Forms | Tablets, injections, capsules, powders, granules, premix, solutions |
| Application Segment | Veterinary pharmaceutical compounding |
| Production Role | Raw active material for finished veterinary dosage forms |
| Storage Condition | Sealed, dry, moisture-protected storage |
| Handling Condition | Handled in compliance with pharmaceutical manufacturing practice to prevent cross-contamination |
As an accredited Zilining Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in sealed moisture-proof bags inside fiber drums, 25 kg net per drum, for veterinary pharmaceutical manufacturing. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Zilining Powder Veterinary Grade API, drum-packed and palletized, for tablet, injection, capsule, powder, granule, premix, and solution production. |
| Shipping | Shipping for Zilining Powder is handled with strict temperature control and moisture-proof, sealed packaging to maintain potency. All shipments comply with veterinary pharmaceutical regulations, with expedited delivery options available. Hazard documentation and tracking are provided for domestic and international orders. |
| Storage | Store Zilining Powder (Veterinary Grade API) in tightly sealed, original containers in a cool, dry, well-ventilated area at controlled room temperature. Protect from light, moisture, and direct sunlight. Avoid exposure to heat or oxidizing agents. Keep away from incompatible materials and out of reach of children. Use clean, dry equipment when handling; reseal immediately after use. |
| Shelf Life | Shelf life indicates the period Zilining Powder veterinary API remains stable, potent, and pure under proper storage conditions before expiration. |
Direct compression of Zilining veterinary tablets requires that the API particle size distribution, moisture content, and bulk density be evaluated before excipient selection, because the powder’s flow function coefficient measured on a ring shear tester determines whether single-stage blending or roll compaction is viable at production scale. Formulations with 5.0% w/w to 80.0% w/w Zilining are processed only when total tablet mass is not less than 80 mg; because published data for this specific configuration are limited, each addition ratio is justified through assay-driven content uniformity trials rather than assumed from compendial precedent. The industry compliance anchor is USP ⟨905⟩ Uniformity of Dosage Units, supported by USP ⟨1217⟩ tablet breaking force and ICH Q3D elemental impurity risk assessment. For downstream production, the API is geometrically diluted into a microcrystalline cellulose and dibasic calcium phosphate dihydrate carrier, blended in a 500 L to 1500 L IBC bin blender, and compressed on a rotary tablet press with precompression force between 5 kN and 10 kN; when sticking or capping appears, press speed is reduced and magnesium stearate is increased from 0.5% w/w to 1.0% w/w, though dissolution retardation must then be rechecked under USP ⟨711⟩ conditions. In plants where relative humidity exceeds 60%, direct compression is replaced by granulation or the blend is held in dehumidified suites below 40% RH to prevent particle agglomeration. The terminal product is a film-coated veterinary tablet, with 2% w/w to 4% w/w polyvinyl alcohol or hydroxypropyl methylcellulose coating applied in a side-vented coating pan to reduce dusting and mask bitter API taste.
Sterile filtration throughput for Zilining injection solutions is governed by the interaction between membrane type, solution viscosity, and dissolved gas content; at concentrations above 10.0% w/v, a polyethersulfone membrane with a 0.22 µm pore size exhibits flux decline beyond 30% after 200 L/m² when the solution temperature is below 20 °C, a production bottleneck observed in campaigns without in-line heat exchange. The addition ratio is formulation-dependent and may range from 2.0% w/v to 20.0% w/v when the active is soluble in the selected vehicle; where published data for this specific configuration are limited, solubility screening in phosphate-buffered saline at 25 °C and 37 °C must precede scale-up. Compounding is typically conducted at 40 °C to 50 °C in water for injection, with pH adjustment using 0.1 M hydrochloric acid or sodium hydroxide to a range confirmed by forced degradation studies; excursions outside that range can produce visible and subvisible particulate matter. Sterile manufacturing is anchored to 21 CFR Part 210/211, EU GMP Annex 1, USP ⟨1⟩, USP ⟨71⟩, USP ⟨85⟩, and USP ⟨790⟩; cleanroom operations follow ISO 14644-1, and compressed air on the filling line must meet ISO 8573-1 Class 1 particle and Class 4 water limits. Downstream production uses a two-stage filtration train with a glass-fiber prefilter followed by a sterilizing-grade 0.22 µm membrane, with integrity testing by forward flow diffusion before and after filling; if terminal steam sterilization at 121 °C for 15 minutes is validated, it is preferred over aseptic filtration because the sterility assurance level targets 10⁻⁶. The terminal product is a sterile injectable solution filled in amber Type I glass vials, with or without an antimicrobial preservative determined by single-dose or multi-dose presentation and preservative efficacy testing.
For encapsulation, the critical parameter is powder flow and plug formation; addition ratios between 10.0% w/w and 70.0% w/w with lactose monohydrate, sodium starch glycolate, and 0.25% w/w to 1.0% w/w colloidal silicon dioxide are processed under USP ⟨711⟩, USP ⟨905⟩, and ICH Q3D using an automatic capsule filling machine at 70% to 90% of fill volume, with weight sorting and sub-batch blending for immediate-release hard-shell veterinary capsules.
When Zilining is dispersed in low-dose oral powders for top-dressing or reconstitution, the particle size differential between the active and the carrier becomes the dominant source of assay variation, because fine API fractions with a median particle size below 50 µm segregate during transit if the carrier particle size is above 500 µm. The addition ratio in oral powder formulations commonly falls between 0.5% w/w and 10.0% w/w, which requires geometric dilution in 1:1 to 1:10 steps before final blending in a tumble mixer operating at 60% to 80% of nominal capacity. Relevant standards include ICH Q2(R2) for analytical method validation, ICH Q3D for elemental impurities, and USP ⟨795⟩ for nonsterile compounding where applicable, while commercially registered veterinary powders follow 21 CFR Part 210/211. Downstream processing involves passing the API through a 500 µm sieve to break agglomerates, pre-blending with a water-soluble carrier such as dextrose or lactose, then filling into sachets with an auger powder filler; fill weight verification is performed at 10-minute intervals because powder flow shifts with ambient humidity. The terminal product is a unit-dose oral powder sachet or a bulk jar with a dosing spoon, intended for reconstitution in drinking water or feed after species-specific dose calculation.
Aqueous granulation of Zilining requires a binder that maintains viscosity below 300 mPa·s at 20 °C; polyvinylpyrrolidone K30 at 3.0% w/w to 8.0% w/w in the granulating solution is selected when the dry blend contains 10.0% w/w to 50.0% w/w API and the target granule loss on drying is below 2.0% after fluid-bed drying at 60 °C inlet temperature. If Zilining is hydrolytically sensitive, a hydroalcoholic granulation with ethanol:water ratios between 50:50 and 80:20 is used to reduce water exposure, but explosion-proof equipment and solvent recovery are mandatory under ATEX workplace safety requirements. Compliance references are USP ⟨711⟩ for dissolution of the finished granules, USP ⟨1217⟩ for tablet breaking force if the granules are compressed, ICH Q3D, and USP ⟨786⟩ for particle size distribution by sieve analysis. Production equipment is a high-shear granulator with a 65 L bowl, chopper speed of 1500 rpm, and impeller speed of 300 rpm, followed by a fluid-bed dryer with product temperature held below 40 °C for heat-labile API. Terminal product is an oral granule for reconstitution or direct administration, packed in low-moisture vapor transmission film with desiccant to maintain moisture below 2.0% at ambient storage.
Unlike tablet or capsule loading, Zilining premix addition ratios are governed by the target final feed concentration and the dilution accuracy of the feed mill, not by a fixed percentage in the premix alone; the API is incorporated into a carrier at 1.0% w/w to 20.0% w/w, and the premix is then diluted into complete feed at 1:100 to 1:1000 according to the authorized species-specific dose. Medicated feed operations handling Zilining premixes must comply with FDA 21 CFR Part 558 or EU Regulation 1831/2003 as applicable, with mixer validation requiring a coefficient of variation below 5% across 10 sampling points and documented flush or cleaning sequences to prevent carryover into non-target feed batches. Downstream production uses a 2000 kg ribbon mixer or paddle mixer with a step-mixing sequence: the active is first blended with 25 kg of carrier, then diluted into 500 kg of intermediate premix, and finally into the target batch. Terminal product is a medicated premix in 20 kg multi-wall paper bags with polyethylene liner, labeled for feed mill use only and not for direct administration without further dilution.
Water-soluble Zilining concentrates present a pH-dependent solubility boundary that must be mapped before setting the final addition ratio, because hard-water cations above 200 mg/L as CaCO₃ can precipitate buffering agents and reduce recovery below 90% of label claim after 24 hours. The concentrate is formulated at 1.0% w/v to 10.0% w/v Zilining, with a citrate or phosphate buffer system, a preservative if multi-dose, and a flavor-masking agent; the addition ratio is adjusted based on the dilution factor specified for drinking water administration. Compliance is established by USP ⟨795⟩ for nonsterile preparations where applicable, ICH Q2(R2) for method validation, and 21 CFR Part 210/211 for commercial finished product. Production involves dissolving Zilining in purified water at 35 °C to 45 °C, cooling to 25 °C, then filtering through a 0.45 µm to 5 µm clarifying filter before filling into amber high-density polyethylene bottles. Terminal product is an oral liquid or water-soluble concentrate for use in automated water medicators at poultry, swine, or companion animal facilities, with tank-mix stability verified at the intended dosing concentration.
Competitive Zilining Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618963613625 or mail to sales10@sinochem-nanjing.com.
We will respond to you as soon as possible.
Tel: +8618963613625
Email: sales10@sinochem-nanjing.com
Flexible payment, competitive price, premium service - Inquire now!
Zilining Powder Veterinary Grade API is released as a white to off-white crystalline powder under product code ZLN-VP-220; the micronized injection-grade variant is designated ZLN-VP-220I and the air-jet-milled solid oral variant is designated ZLN-VP-220M. The material is qualified for manufacture of tablets, capsules, oral powders, granules, medicated premixes, and injectable solutions after route-specific processing. Unlike feed-grade premixes, the API contains no calcium carbonate, corncob, or vermiculite carrier; assay normalization is performed on the dried basis, and residual water content is controlled to prevent hydrolysis in moisture-sensitive granulation lines. Batch release includes high-performance liquid chromatography assay, related substances, loss on drying, heavy metals, residual solvents, microbial enumeration, and, for injection-grade lots, bacterial endotoxins. Packaging is double low-density polyethylene liners in 25 kg net fibre drums. The API is manufactured under ICH Q7 active substance GMP principles and is suitable for Type A medicated article downstream use where 21 CFR 226 applies.
For each dosage route, acceptance limits are route-specific rather than a single superficial specification. The oral tablet and capsule grade permits a particle-size D90 up to 150 µm because downstream wet milling and granulation reduce segregation risk; the injection-grade lot is controlled to D90 ≤ 75 µm to allow rapid wetting and to meet subvisible particle limits after dissolution. Assay by HPLC against a reference standard uses an octadecylsilyl column 250 × 4.6 mm, 5 µm with detection at 254 nm; the acceptance window for Zilining on the dried basis is 98.5–101.5%. Related substances are controlled as any individual unspecified impurity ≤ 0.5% and total impurities ≤ 2.0%. Loss on drying is ≤ 1.0% for solid oral use, but the injection-grade powder is tightened to ≤ 0.5% to avoid hydrolysis and headspace moisture uptake in vials.
| Parameter | Method / standard | Release limit or range | Applicable route |
|---|---|---|---|
| Appearance | Visual inspection | White to off-white crystalline powder | All |
| Assay on dried basis | HPLC, CPV 2020 General Chapter 0512 | 98.5–101.5% | All |
| Loss on drying | CPV 2020 General Chapter 0831 | ≤ 1.0% solid oral; ≤ 0.5% injection | Route-specific |
| Related substances | HPLC area normalization | Single unspecified ≤ 0.5%; total ≤ 2.0% | All |
| Particle size D90 | Laser diffraction, ISO 13320:2020 | ≤ 75 µm injection; ≤ 150 µm oral | Route-specific |
| Bulk / tapped density | USP <616> Method I | 0.40–0.55 g/mL; 0.60–0.75 g/mL | Tablets, capsules, premix |
| Bacterial endotoxins | CPV 2020 General Chapter 1143 | < 0.50 EU/mg injection; < 5.0 EU/g oral | Injection / oral |
| Microbial enumeration | CPV 2020 General Chapters 1105 / 1106 | TAMC ≤ 10² CFU/g; TYMC ≤ 10¹ CFU/g; Escherichia coli absent | All non-sterile |
| Residual solvents | Headspace GC, VICH GL18 | Acetone ≤ 5000 ppm; ethyl acetate ≤ 5000 ppm; methanol ≤ 3000 ppm; Class 1 not detected | All |
These release limits are selected to maintain compendial alignment, not to guarantee clinical efficacy in a particular target species; efficacy is established by the downstream veterinary product’s regulatory file. The injection-grade lot, in addition to the solid oral profile, is controlled for subvisible particulate matter after reconstitution and for sterility when the downstream process does not include terminal sterilization. For oral powders and premixes, microbial enumeration is the critical safety parameter because these products are administered via feed or drinking water and may be stored in farm bins at high humidity.
Laser diffraction data for three consecutive production lots show D10 4.2 µm, D50 52 µm, D90 143 µm, span 2.7, bulk density 0.46 g/mL, tapped density 0.68 g/mL, Hausner ratio 1.48, and Carr index 32%. That places the unprocessed powder at the passable-to-poor flow boundary under USP <1174>; direct compression formulations therefore require 0.5 wt% colloidal silicon dioxide or 1.0 wt% magnesium stearate to maintain die-fill consistency at press speeds above 25 rpm. The powder is not suitable for direct compression without flow aid because its low bulk density and high fine fraction produce static adhesion on tableting dies.
Tablet compression on a 16-station rotary press with 10 kN main compression and 3 kN precompression reveals capping when moisture content falls below 0.5% or when turret speed exceeds 35 rpm without prior dry granulation. The failure mode is consistent with brittle fracture and low tensile strength rather than punch sticking; replacement of direct compression with roller compaction at roll pressure 6 MPa and screen 1.0 mm restores tablet hardness to 80 N and friability below 0.8% per CPV 2020 0923. These thresholds define the processing window for tablet manufacturers: maintain water content between 0.8% and 1.0% before compression, add the lubricant no earlier than 3 min before tableting, and monitor ejection force; values above 1.8 kN indicate excessive die-wall friction. Direct compression formulations that omit roller compaction often fail friability testing at high press speeds even when the powder meets the oral particle-size specification.
For capsule filling, the same oral powder is dry-mixed with lactose monohydrate to a bulk density of 0.55 g/mL; filling on a dosator machine generates acceptable weight variation below 3.0% RSD when the powder bed depth is kept constant. Powder transfer through dilute-phase pneumatic conveying should be avoided because fines below 10 µm may blind cartridge filters and shift D90 in the dosing hopper. Where granules are required, a wet granulation endpoint of 45–55% w/w mass consistency in a high-shear mixer impeller at 400 rpm and chopper at 1500 rpm yields granules with D50 180–250 µm and residual moisture 1.5–2.0% after fluid-bed drying at 55 °C inlet air. Granulation is preferred when the API is combined with hygroscopic carriers or when tablet presses operate above 40 rpm.
Zilining Powder Veterinary Grade API intended for injectable solution manufacture is lot-designated ZLN-VP-220I and requires a bacterial endotoxin level < 0.50 EU/mg by kinetic chromogenic assay per CPV 2020 1143. Reconstitution in water for injection at 25 °C under aseptic conditions should be followed by sterile filtration through a 0.22 µm polyethersulfone membrane; if the solution is terminally sterilized, the thermal exposure at 121 °C for 15 min must be validated because the API may undergo pH-dependent hydrolysis above 6.5. The solution is typically compounded at pH 4.5–6.5 using citrate or acetate buffer; phosphate buffers can precipitate if calcium or magnesium ions are present in the water system. Subvisible particulate matter after reconstitution is controlled by CPV 2020 0904 / USP <788>: not more than 6000 particles per container at ≥ 10 µm and not more than 600 particles per container at ≥ 25 µm for small-volume injections. Because this API is supplied as a dry crystalline powder, hydrolytic degradation in the packaged state is lower than a ready-to-use solution; after reconstitution, the product should be used within 24 h unless stability data support longer storage at 2–8 °C.
Published solubility data for Zilining in mixed organic-aqueous injection vehicles is limited; therefore formulation work should begin with saturation shake-flask determinations per EP 5.11 before selecting co-solvent ratios. The injection-grade powder should not be combined with strong oxidizing agents or with amine-based additives at alkaline pH because these conditions accelerate degradation of the active moiety. If the drug substance is dissolved at temperatures above 50 °C, the vessel must be blanketed with nitrogen and protected from light, and the solution must be cooled to 25 °C within 4 h to avoid thermal degradation.
Medicated premixes prepared from this API typically dilute the active substance into calcium carbonate, lactose monohydrate, or wheat middling carriers at inclusion rates from 1 kg/tonne to 10 kg/tonne depending on target species and regulatory status. Residual solvent limits follow VICH GL18; methanol is limited to 3000 ppm, acetone to 5000 ppm, and ethyl acetate to 5000 ppm. Class 1 solvents are not detected by headspace gas chromatography with flame ionization detection and a limit of quantitation of 5 ppm. Heavy metals are controlled as lead not more than 10 ppm and arsenic not more than 2 ppm by CPV 2020 0821 Method II and 0822, respectively. These limits are tighter than those commonly accepted for technical-grade material and are intended to avoid accumulation in target tissues after oral administration in food-producing species. The powdered API should not be mixed with acidic or alkaline premix carriers that alter local pH beyond 4.0–8.0 unless full stability data are available.
| Attribute | Zilining Powder Veterinary Grade API ZLN-VP-220 | Feed-grade premix, carrier-diluted | Unprocessed technical powder |
|---|---|---|---|
| Assay on dried basis | 98.5–101.5% | 5–20% active dispersed on carrier | Variable, commonly 90–98% with undefined impurities |
| Particle size D90 | ≤ 75 µm injection; ≤ 150 µm oral | 300–800 µm, carrier-dependent | Not controlled |
| Loss on drying | ≤ 0.5–1.0% route-specific | 8–12% carrier moisture | ≤ 2.0% typical, but not route-specific |
| Endotoxin | < 0.50 EU/mg injection; < 5.0 EU/g oral | Not routinely tested | Not controlled |
| Microbial enumeration | TAMC ≤ 10² CFU/g; TYMC ≤ 10¹ CFU/g | TAMC up to 10⁴ CFU/g | Not controlled |
| Residual solvents | VICH GL18 Class 3 limits | May contain carrier-drying solvent residues | Process solvents not always characterized |
Compared with a ready-to-use injectable solution, Zilining Powder Veterinary Grade API reduces hydrolytic degradation during storage but shifts the burden of aseptic processing to the downstream manufacturer. Compared with feed-grade premix, the API allows precise dose titration, reduces carrier-related microbial load, and avoids the analytical interference of carrier-derived pigments and sugars. However, the API is not intended for direct administration without dilution; it must be formulated into a finished dosage form or medicated premix according to the target species label.
Batch-to-batch variability in particle size D90 observed across 5 consecutive production lots ranged from 86 µm to 143 µm, which is acceptable for solid oral dosage forms after wet granulation but too broad for direct injection reconstitution without pre-filtration. Therefore, injection-grade material is air-jet milled to D90 ≤ 75 µm and then vacuum-dried at 45 °C for 6 h to reduce solvent and moisture below the tightened loss-on-drying criterion. During that milling step, the crystalline habit is retained; X-ray powder diffraction indicates no polymorph conversion when the inlet air temperature is maintained below 50 °C. Exceeding 50 °C during micronization may increase the amorphous fraction, which in turn raises hygroscopicity and reduces reconstitution clarity. This is a critical threshold for injectable grade manufacture.
For solution dosage forms used in drinking water, the API should be pre-dispersed in 10 volumes of water at 30–35 °C with gentle agitation; high-shear mixing above 1000 rpm can entrain air and generate foam that slows transfer through 0.22 µm filters. Solutions with final concentration above 5 mg/mL may require pH adjustment with 0.1 M citric acid to remain clear; precipitation at the proportioner nozzle indicates that hardness ions in the dilution water exceed 200 mg/L as calcium carbonate and should be treated with a chelating agent. These operational boundaries apply to field-use preparation and should be validated with the specific water quality on each farm.
Storage at 25 °C and 60% relative humidity in sealed aluminum laminate with desiccant has been used to maintain retest attributes for 36 months. Protect from light and moisture; do not repackage into unlined paper sacks. The retest interval is not a shelf-life extension for finished veterinary products; downstream regulatory stability protocols remain the responsibility of the finished dosage manufacturer.