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Gongying Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    • Product Name: Gongying Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 515261
    Product Name Gongying Powder Veterinary Grade API
    Active Ingredient Gongying (Taraxacum) extract powder
    Physical Form Fine dry powder
    Color Brownish-yellow to light greenish-brown
    Odor Characteristic herbal and slightly bitter odor
    Solubility Sparingly soluble in cold water; soluble in hot water and dilute ethanol
    Microbial Limits Total aerobic count ≤ 1000 CFU/g; no Salmonella or E. coli in 10 g
    Veterinary Grade API grade suitable for veterinary pharmaceutical formulation
    Suitable Dosage Forms Tablets, injections, capsules, powders, granules, premix, solutions
    Storage Conditions Store in tightly sealed containers in a cool, dry, well-ventilated place
    Shelf Life 24 months when stored under recommended conditions

    As an accredited Gongying 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 & Storage
    Packing Gongying Powder Veterinary Grade API is packed in sealed double-layer polyethylene bags inside fiber drums, 25 kg net weight per drum.
    Container Loading (20′ FCL) Container Loading (20′ FCL): One 20-foot container securely loads palletized, sealed drums of Gongying Powder veterinary grade API for various formulations.
    Shipping Shipped in sealed, moisture-proof packaging with tamper-evident labels, compliant with veterinary API transport regulations. Temperature-controlled options available. Requires proper documentation, customs declaration, and handling by certified logistics partners. For veterinary use only; not for human consumption or clinical research.
    Storage Store Gongying Powder Veterinary Grade API in its original, tightly sealed container in a cool, dry, well-ventilated area, ideally below 25°C. Protect from light, moisture, and heat. Keep away from strong oxidizers and incompatible substances. Do not freeze. Ensure container remains clearly labeled and closed when not in use. Use appropriate personal protective equipment when handling.
    Shelf Life Shelf life is 24 months from manufacture, provided the powder remains sealed, stored in a cool, dry place, and protected from sunlight.
    Application of Gongying Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    In a closed-house broiler operation with a 2,000 L header tank and a 24-hour water intake of 3,800–4,200 L, Gongying Powder Veterinary Grade API is processed into a soluble oral powder rather than dry-administered to avoid feed refusal from the fine herbal particulate. The batch is dry-blended in a 250 kg double-ribbon mixer at 18–20 rpm for 15 minutes after a 1:10 pre-blend step, using 20.0 wt% API powder, 78.0 wt% anhydrous dextrose, and 2.0 wt% povidone K30 as dispersing binder. This pre-blend is then diluted in drinking water at a final working concentration of 1.0–2.0 g API powder per litre, with the exact point within the range calculated from the batch cichoric acid assay; for a typical 2.5% cichoric acid assay the resultant water contains 25–50 mg cichoric acid per litre. The reconstituted solution remains homogeneous for 24 hours at 15–25°C when protected from direct ultraviolet exposure; above 30°C the degradation rate of the marker compound increases by 15–20% and fine sediment can block nipple drinker cup valves. Industry compliance is governed by Directive 2001/82/EC for EU marketing and 21 CFR 520 for water-soluble veterinary powders in the United States, with stability in the final commercial container evaluated according to VICH GL18 at 15–25°C for 24 hours after reconstitution. The production process requires a terminal sieve of 100 mesh (≤150 μm) to prevent proportioner diaphragm blockage, and the unpacked sachets are heat-sealed in 100 g and 1 kg aluminium-foil pouches. Terminal finished product types are water-soluble oral powders for poultry and swine, supplied as single-dose and multi-dose sachets for direct addition to drinking water systems.

    What Limits the Uniformity of a 1.0% Feed Premix When the API Particle Size Is Not Controlled?

    In feed-mill production, the API powder is incorporated into a calcium carbonate or rice-hull carrier at 5.0–20.0 wt% to form a veterinary premix, then metered into complete feed at 1.0–10.0 kg per tonne. The limiting variable is not the active marker but the particle-size mismatch between the botanical powder, which has a D90 of 150–250 μm if unmicronized, and the carrier with a D50 of 180–220 μm, because this mismatch produces elutriation segregation during pneumatic transfer. A 1.0-tonne double-ribbon mixer with 60–70% working fill and 20 rpm rotation achieves blend coefficient of variation ≤5.0% only when the API powder is pre-sieved through 60 mesh (≤250 μm) and pre-blended for 3 minutes with an equal mass of carrier before the main mixing step of 12 minutes. The formulation addition ratio is arithmetic: a 5.0 wt% premix metered at 2.0 kg/tonne yields 100 mg API powder per kg complete feed and 2.5 mg cichoric acid per kg when the assay is 2.5%. Industry compliance for EU feed businesses is Regulation (EC) No 183/2005 feed hygiene, GMP+ BA2 feed safety assurance, and ISO 22000 prerequisite programmes; in the United States, medicated feed premixes require 21 CFR 558.4 cGMP and an approved VFD or NADA classification. Downstream production uses a micro-dose bin with mass-flow hopper and loss-in-weight feeder to control premix addition to ±2% of target. Terminal finished product types are 1.0%, 2.5%, and 5.0% veterinary premixes in 25 kg paper sacks with polyethylene liner, intended for on-farm mixing into swine and poultry rations.

    API powder concentration in premix (% w/w)Premix inclusion (kg/tonne feed)Final API powder in complete feed (mg/kg)Cichoric acid in complete feed at 2.5% assay (mg/kg)
    5.02.01002.5
    10.02.02005.0
    20.01.02005.0
    20.02.550012.5

    For oral granules intended for piglet drenching and top-dressing, the API powder is agglomerated in a fluid-bed top-spray granulator with a 120 kg batch vessel. The dry binder matrix consists of 40.0–55.0 wt% API powder, 35.0–50.0 wt% maltodextrin DE 15–20, and 5.0–10.0 wt% sorbitol; a 5.0% povidone K30 aqueous binder solution is sprayed at 8–12 g/min/kg dry charge with inlet air at 55–65°C and product temperature held at 30–35°C. If the product temperature exceeds 35°C during the binder spray, the maltodextrin matrix becomes tacky and the yield of 16–60 mesh granules falls below 70%. After granulation, the material is dried to moisture ≤5.0% and sieved through 16 mesh (≤1.18 mm) and 60 mesh (≥250 μm) to remove fines, because retention of fines above 25% of batch mass raises the angle of repose to >40° and blocks the volumetric dosator. The addition ratio in the final granule is set by a marker-based calculation: if the API assay is 2.5% cichoric acid and the target granule is 1.0 mg cichoric acid per 100 mg granule, then 40.0 g API powder is required per 100 g dry granule matrix before granulation losses. Industry compliance includes Ph. Eur. 2.9.36 powder flow, Ph. Eur. 2.9.40 uniformity of dosage units, and microbial limits for oral veterinary preparations under Ph. Eur. 5.1.4 category 3B. The process air is dehumidified to RH ≤30% for the final 10 minutes to prevent hygroscopic collapse of the maltodextrin carrier. Terminal finished product types are oral granules in 100 g, 500 g, and 1 kg foil-lined composite jars, plus 20 g sachets for single-animal administration after reconstitution in water.

    Direct Compression Boundary Conditions for High-Dose Herbal API Tablets

    Direct compression of the API powder into companion-animal tablets becomes process-critical when the API fraction exceeds 40.0 wt% because the fibrous botanical particles dominate the deformation behaviour of the compact. The formulation addition ratio is 40.0–65.0 wt% API powder, 20.0–35.0 wt% microcrystalline cellulose PH102, 3.0–5.0 wt% croscarmellose sodium, 0.5–1.0 wt% magnesium stearate, and 0.5–1.5 wt% colloidal silicon dioxide; for a 1,200 mg oblong tablet containing 50.0 wt% API powder at 2.5% cichoric acid assay, the delivered marker is 15.0 mg cichoric acid per tablet. The downstream production process uses a 29-station rotary press with 19.0 × 8.5 mm tooling, precompression 6–10 kN, main compression 18–25 kN, and target tablet hardness 80–120 N. Under these conditions the ejection force remains below 1,000 N and friability is ≤1.0%; if the API powder bulk density drops below 0.45 g/cm³, the feed shoe fill depth must be increased to 20–24 mm to maintain weight variation CV ≤3.5%. A 60-minute disintegration time is typical when croscarmellose is kept at 4.0 wt%; increasing croscarmellose to 5.0 wt% shortens disintegration to 35 minutes but reduces tablet hardness by approximately 12%. Industry compliance includes USP <905> uniformity of dosage units, USP <1217> tablet breaking force, Ph. Eur. 2.9.7 disintegration, and 21 CFR 211 cGMP for finished pharmaceutical dosage forms. Terminal finished product types are uncoated and film-coated tablets for canine and feline oral administration, filled into 100- and 500-count HDPE bottles with 1 g silica-gel desiccant.

    When Injectables Are Compounded From Powdered Herbal Extract, pH and Endotoxin Load Govern Sterile Filtration

    Parenteral processing of this API powder begins with a water extraction at 60–70°C for 2 hours, not with direct reconstitution of the whole-herb powder, because insoluble plant cell fragments above 10 μm would exceed injectable particulate limits under USP <788> and Ph. Eur. 2.9.19. The extract is cooled to 20–25°C, clarified through a 0.45 μm polypropylene depth filter, then sterile-filtered through a 0.22 μm PVDF membrane. The formulation addition ratio is determined by extraction efficiency and final marker concentration. At a batch assay of 2.5% cichoric acid and an extraction recovery of 60%, a target solution of 0.5 mg/mL cichoric acid requires 33.3 g API powder per litre; if the batch assay falls to 2.0%, the powder charge rises to 41.7 g/L. The filtrate is adjusted to pH 6.5–7.5 with 1.0 M sodium hydroxide or hydrochloric acid, made isotonic with 0.9% sodium chloride, and filled into 50 mL and 100 mL type II glass vials with bromobutyl rubber stoppers. Terminal sterilisation at 121°C for 15 minutes is acceptable only if stability data demonstrate no marker loss greater than 10%; otherwise aseptic filtration is used and the line must be validated to a sterility assurance level of 10⁻⁶ under 21 CFR 212 for veterinary APIs and Ph. Eur. 5.1.1. Bacterial endotoxin is controlled below 0.5 EU per mg extract using Ph. Eur. 2.6.14; if the crude powder endotoxin burden exceeds the water extract capacity, the powder is pre-washed with 70% ethanol and vacuum-dried at 40°C before extraction. Terminal finished product types are parenteral solutions for cattle and swine, supplied as multi-dose vials and further diluted into isotonic saline before intramuscular or subcutaneous administration.

    Capsule Filling and Powder Segregation: A Process Window Defined by Flowability

    Encapsulation of the API powder is limited by its cohesive botanical fines, which produce a Hausner ratio of 1.35–1.55 and a compressibility index of 25–35%, making direct dosator filling without a glidant unacceptable. The formulation addition ratio for Size 0 hard gelatin capsules is 45.0–70.0 wt% API powder, 20.0–40.0 wt% microcrystalline cellulose PH105, 2.0–4.0 wt% sodium starch glycolate, 0.5 wt% magnesium stearate, and 0.5–1.0 wt% fumed silicon dioxide; a 450 mg fill weight at 55.0 wt% API powder delivers 247.5 mg API powder and 6.2 mg cichoric acid when the assay is 2.5%. The downstream production process runs on an intermittent-motion capsule filler at 70,000–90,000 capsules per hour, with tamping pins set to 12–15 mm and vacuum assisted to retain powder plug integrity. The filling room is held at 35–45% RH and 20–22°C because moisture above 8.0% in the API powder increases stickiness on the dosator pins and raises fill weight variability above CV 4.0%. Industry compliance includes USP <905> uniformity of dosage units, Ph. Eur. 2.9.36 powder flow, Ph. Eur. 2.9.42 dissolution for solid oral botanical preparations, and 21 CFR 211 cGMP. Terminal finished product types are oral capsules for companion animals and equine use, packaged in PVC/PVDC blister strips and 10-strip cartons, with a desiccant canister when supplied in bulk containers.

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    Certification & Compliance
    More Introduction

    Gongying Powder is a non-sterile veterinary active pharmaceutical ingredient supplied as a white to off-white crystalline powder under model designation GP-VET-API-100. A micronized variant, GP-VET-API-100M, is available for suspension concentrates, injectable pre-filtration processing, and low-dose dry powder blends where content uniformity is sensitive to particle size distribution. The powder is packaged in sealed low-density polyethylene liners inside aluminum foil laminate bags at a net weight of 25 kg; custom packaging for aseptic transfer is available on request. Storage in unopened original containers is controlled room temperature not exceeding 25 °C, protected from light and moisture. Opened containers should be used within 30 days when stored at or below 60% RH; the lot-specific re-test interval is typically 24 months from manufacture. The material is not intended for direct administration and must be further processed under applicable veterinary GMP into tablets, capsules, injections, solutions, powders, granules, or premixes.

    Incoming quality control should confirm identity by infrared spectroscopy or HPLC retention time, water content, particle size, and appearance before release to production. The active substance is not diluted with carriers, flow aids, or preservatives; therefore the mass balance in downstream formulation remains with the formulator.

    Release specifications are lot-specific and route-dependent. The following representative framework is based on current Chinese Veterinary Pharmacopoeia and selected Ph. Eur. general chapters; it is not a substitute for the approved dossier.

    ParameterAcceptance criterionTest method
    Appearancewhite to off-white crystalline powdervisual examination
    Identificationmatches reference IR spectrum and HPLC retention timecompendial IR and HPLC methods
    Loss on drying≤ 0.5%Ph. Eur. 2.2.32 or equivalent CVP method
    Residue on ignition≤ 0.1%current CVP general method
    Heavy metals≤ 10 ppmPh. Eur. 2.4.8 or equivalent CVP method
    Related substancestotal impurities ≤ 1.0% unless the active substance monograph specifies otherwisestability-indicating HPLC; system suitability per Ph. Eur. 2.2.29
    Assay (dried basis)98.0%–102.0% or as specified in the approved dossiercurrent CVP monograph HPLC
    Particle sizeD90 ≤ 250 µm for dry blending; D90 ≤ 75 µm for GP-VET-API-100Mlaser diffraction, ISO 13320:2020
    Residual solventsconforms to VICH GL18 class limits; results are lot-specificPh. Eur. 2.4.24
    Microbial limitsTAMC ≤ 100 CFU/g, TYMC ≤ 10 CFU/g for non-sterile oral gradesPh. Eur. 2.6.12
    Bacterial endotoxinsoptional reduced-endotoxin grade, limit calculated from maximum daily dosePh. Eur. 2.6.14

    Assay of the active substance is performed by HPLC using a stability-indicating method. Method suitability requires resolution between the main peak and known related substances not less than 2.0, tailing factor not more than 2.0, and relative standard deviation for replicate injections not more than 1.0%. Residual solvent analysis uses headspace gas chromatography; method quantification limits are established for Class 1 and Class 2 solvents per VICH GL18.

    What Processing Constraints Appear in Direct Compression and Wet Granulation?

    Direct compression of GP-VET-API-100 requires pre-blending with microcrystalline cellulose, croscarmellose sodium, and magnesium stearate. Rotary tablet presses with 10 mm to 12 mm round flat-faced or standard concave tooling are used for development batches. Because the powder may exhibit an angle of repose above 40°, wet granulation is often preferred for higher-dose tablets. High-shear granulation is performed with an impeller tip speed of 2 m/s to 6 m/s and a chopper speed of 1000 rpm to 2000 rpm; these settings are starting points and require pilot confirmation because published data for this specific product under high-shear granulation is limited.

    Wet massing endpoint is determined by impeller torque or power draw rather than fixed time; over-granulation produces fines and low-compressibility agglomerates. The wet mass is dried in a fluid-bed dryer with inlet air temperature not exceeding 60 °C unless forced-degradation data support higher exposure. Product temperature is monitored, and discharge moisture content is confirmed by loss on drying; a common target is 1% to 3%. Dried granulate is milled through a screen size of 1.0 mm and lubricated with 0.5%–1.0% magnesium stearate. Higher lubricant levels prolong disintegration time. Tablet hardness is adjusted in the range of 50 N to 80 N only after dissolution data confirm an acceptable release profile, because the API itself does not dictate a fixed hardness. Dissolution testing follows Apparatus 2 paddle at 50 rpm to 75 rpm in pH-adjusted media as described in the relevant veterinary monograph.

    For capsules, granulate flow is quantified by Carr index and Hausner ratio; a Carr index below 20% is generally acceptable for automatic dosator or tamping disk filling. If flow is insufficient, the formulator may add colloidal silicon dioxide at 0.2%–0.5%, but this addition must be validated for content uniformity and dissolution.

    Residual solvent analysis uses headspace gas chromatography with flame ionization or mass spectrometric detection. A 30 m × 0.25 mm × 1.4 µm 6% cyanopropylphenyl/94% dimethylpolysiloxane capillary column is a common screening configuration, but method suitability must be confirmed for the specific active substance. Class 1 solvents are controlled below the limits defined in VICH GL18; Class 2 solvents are reported against the same guidance. Peak purity for HPLC assay is evaluated by photodiode array detection from 200 nm to 400 nm; if the chromophore is weak, charged aerosol detection or evaporative light scattering may be required. The supplier certificate of analysis should include retention time, purity factor, and resolution from the nearest known related substance. X-ray powder diffraction may be used to confirm the polymorphic form if the active substance is crystalline, because different crystal forms can alter dissolution kinetics in tablet and suspension formulations.

    Loss on drying and water content are distinct parameters: loss on drying may capture residual solvents and bound moisture, while Karl Fischer titration gives water specifically. For hygroscopic powders, water content above 2.0% may require pre-drying in a vacuum dryer at 40 °C to 50 °C until water content falls below 1.0%; however, the thermal stability of the active substance must be confirmed before drying. Published data for the specific active substance in Gongying Powder under vacuum drying is limited, so a pilot drying study is required.

    Endotoxin and Membrane Compatibility Boundaries for Injection Solutions

    For injectable dosage forms, the API is not sterile as supplied. The active substance is dissolved in Water for Injection under a controlled environment, then clarified and subjected to sterilizing filtration through a 0.22 µm polyethersulfone or polyvinylidene fluoride membrane. Membrane binding studies are required because low concentrations of the active substance may adsorb to some filter materials. Terminal moist heat sterilization at 121 °C for 15 minutes is applicable only after product-specific stability studies; if the active substance degrades under saturated steam, a lower-temperature cycle may be considered but must still meet the sterility assurance level required by the finished product monograph. Published data for this specific configuration is limited, so the manufacturer’s technical file and forced-degradation studies should be consulted before fixing the sterilization cycle.

    Endotoxin limits are dose-dependent. The reduced-endotoxin grade is released with a bacterial endotoxin test performed according to Ph. Eur. 2.6.14, and the acceptance criterion is calculated from the maximum daily parenteral dose. Standard non-sterile oral/feed grades may contain higher bioburden and should not be used in injectable formulation without endotoxin reduction steps. Aseptic processing routes require environmental monitoring and process simulation under applicable GMP provisions; the API itself cannot compensate for inadequate aseptic technique.

    For drinking water solutions, a stock solution is prepared at a concentration below the solubility limit of the active substance in non-chlorinated potable water below 30 °C. Gentle stirring at 20 °C to 30 °C is preferred over high-shear mixing to avoid foam formation. Chlorinated potable water can be used only if chlorine demand studies show no rapid degradation; free chlorine above 2 ppm may reduce assay in some active substances, so the water source should be tested. Hard water containing more than 300 ppm calcium carbonate equivalent may reduce solubility or accelerate precipitation; a jar test with the target water source is therefore part of preformulation. Solutions without a validated preservative system should be used within 24 hours after preparation to avoid microbial proliferation and potency loss.

    When the Powder Is Compounded into Premix and Medicated Feed, What Homogeneity and Thermal Limits Apply?

    Premix preparation requires geometric dilution with a low-moisture carrier such as calcium carbonate, corncob meal, or lactose monohydrate. The active concentration in the intermediate premix is typically 10 g/kg to 100 g/kg depending on the dosage regimen; the final feed carryover rate must be validated against mixer characteristics. Ribbon blenders or double-cone blenders are acceptable if mixing time and fill volume are validated by sampling at 10 evenly distributed points and assaying active content. A coefficient of variation below 5% is commonly required for medicated feed premixes, and first- and last-discharge samples must be verified to rule out segregation. If segregation occurs, the carrier particle size distribution should be adjusted or a flow conditioner added.

    Dry carrier selection matters: porous carriers may absorb hygroscopic API and improve stability, but may also retard dissolution if the carrier binds the active substance. The selected carrier must be tested for pH, moisture, and heavy metals; carriers with high moisture can initiate hydrolysis during storage. If the active substance is light-sensitive or hygroscopic, the premix should be packaged in opaque, foil-lined bags and stored with desiccants to keep final moisture content below 5%.

    Feed pelleting or extrusion can expose the API to frictional heat of 70 °C to 90 °C for 10 s to 30 s. If thermal degradation is observed by assay and related substances, the premix should be applied post-pellet by spraying onto cooled pellets or mixed into the finished mash feed. Because published data specific to Gongying Powder in extruded feed is limited, pilot-scale recovery studies are indispensable before routine production. The recovery assay should include a related substances determination, not only an active content assay, to detect trace degradation products that may affect safety or stability.

    Compared with unmicronized APIs, the micronized GP-VET-API-100M lot has a finer particle size distribution and higher specific surface area; this may reduce disintegration time in tablets and support suspension uniformity, but it also increases electrostatic charge and dust generation. Processing areas should therefore include local exhaust ventilation or containment booths with dust collection. Unlike technical-grade raw powders, this product is released against a veterinary API specification that includes related substances, residual solvents, and microbial limits. Technical or feed additive grades may not carry the same batch-to-batch documentation; the absence of a full API release dossier means those materials can contain unidentified impurities or solvent residues that are not acceptable for injectable or food-producing animal use. A further difference is the absence of added carriers, glidants, or flavorings in GP-VET-API-100. A commercial water-soluble powder may already contain glucose, citric acid, or surfactants, which can simplify drinking water use but reduces flexibility in dose-tailored formulations. For parenteral routes, the optional reduced-endotoxin grade is the principal distinction; if not specified, standard non-sterile oral-grade material should not be used in injectable formulation. Each delivered lot includes a certificate of analysis under ISO 9001:2015 or equivalent quality management system, linking results to specific compendial methods and batch records. When a receiving site audited under EU GMP Part II or equivalent is used, the audit report may be requested; the API supplier should provide an open communication pathway for quality queries and lot-specific deviations.

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