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

    • Product Name: Houyanjing Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions
    • Factroy Site: Zhanjiang, Guangdong, China
    • Price Inquiry: sales10@ascent-petrochem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 637226
    Productname Houyanjing Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions
    Producttype Veterinary-grade active pharmaceutical ingredient (API)
    Grade Veterinary Grade
    Physicalform Powder
    Compatibledosageforms Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions
    Category Veterinary API for formulation use
    Appearance Fine powder
    Color Off-white to light yellow (typical)
    Odor Characteristic mild odor (typical)
    Purity ≥98% (typical; batch-specific certificate required)
    Solubility Water-soluble or dispersible depending on formulation (typical)
    Storageconditions Cool, dry, protected from light
    Shelflife 24 months (typical when stored as directed)
    Packaging 25 kg fiber drum with double polyethylene liner (typical bulk packaging)
    Usage For formulation into veterinary tablets, injections, capsules, powders, granules, premix, and solutions
    Targetspecies Livestock, poultry, and companion animals as approved by local regulation
    Regulatorystatus Veterinary API; use under licensed veterinary supervision and local regulations
    Countryoforigin China (typical)
    Certification GMP-compliant production (typical; verify with supplier)
    Moq Negotiable and supplier-dependent

    As an accredited Houyanjing 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 Houyanjing veterinary-grade API supplied in 25 kg double polyethylene-lined fiber drums, securely sealed and labeled for bulk pharmaceutical use.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Houyanjing Powder Veterinary Grade API in 20-foot container, suitable for tablets, injections, capsules, powders, granules, premix, solutions.
    Shipping Houyanjing Powder Veterinary Grade API is shipped in sealed, moisture-resistant drums or foil-lined bags, labeled per veterinary API and transport regulations. Store cool, dry, away from light. Use qualified carriers; provide SDS, COA, and packing list. Temperature-controlled options available if required. Handle as veterinary API and maintain documentation.
    Storage Store Houyanjing Powder Veterinary Grade API in a cool, dry, well-ventilated area, protected from direct sunlight, moisture, and heat. Keep containers tightly closed, clearly labeled, and upright. Maintain temperature and humidity per manufacturer’s instructions, typically 15–25°C. Segregate from food, feed, and incompatible substances to prevent contamination. Follow SDS, label, and local regulations. Observe shelf life. Do not store near oxidizers or acids.
    Shelf Life Houyanjing Powder Veterinary Grade API typically has 24–36 months shelf life when stored cool, dry, sealed; confirm batch COA.
    Application of Houyanjing Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    For mass medication of broiler, layer, and turkey flocks through the drinking-water route, Houyanjing Powder Veterinary Grade API is first converted into a water-dispersible oral powder rather than being directly dissolved, because the extract contains poorly wettable lignified plant fragments that float and create uneven dosing in nipple drinker systems. The formulation addition ratio is typically 0.5 g/L to 2.0 g/L of final drinking water, with the upper limit reserved for acute respiratory outbreak protocols and the lower limit applied in prolonged prophylactic cycles; the ratio is expressed as extract weight per liter and must be re-calculated per batch using the marker compound assay for total flavonoids, because raw botanical extract lots vary in density by ±8%. Published data for this specific configuration is limited, so the exact addition ratio is validated by the downstream manufacturer’s stability protocol rather than taken from compendial fixed values. In industry compliance terms, this application falls under non-sterile oral veterinary medicinal product requirements: EU Regulation 2019/6, VICH GL1 for analytical method validation, VICH GL2 for stability protocols, Ph. Eur. monograph 5.1.4 for microbiological quality of non-sterile products, and EU GMP Annex 2 for active substance handling. Downstream production equipment is typically a 500 kg ribbon blender or high-shear ploughshare mixer operated at 25 rpm for 8 min with a preblend stage: the extract is first combined with dextrose monohydrate at a 1:10 ratio, then with anhydrous citric acid at 0.5% to 1.0% to buffer alkaline water hardness and reduce oxidation of phenolic marker compounds. The preblend is sieved through a 500 µm conical mill and packed into foil-lined heat-sealed sachets under ≤30% relative humidity. Finished dosage forms include 100 g, 500 g, and 1 kg water-soluble powder sachets, as well as dosing-pump liquid concentrates reconstituted farm-side; the powder form is specified for export because its water activity is maintained below 0.60, which limits microbial proliferation during tropical shipping without requiring cold-chain logistics.

    What sterility assurance level applies to Houyanjing injection manufacturing?

    Terminally sterilised injectable solutions containing Houyanjing Powder require a sterility assurance level of 10−6 per Ph. Eur. 5.1.1 and EU GMP Annex 1; if the powder is aseptically filtered without terminal heat, the process must be validated with media fills under ISO 14644-1:2015 Class 5 conditions. The formulation addition ratio for parenteral solutions ranges from 2.0% w/v to 10.0% w/v of extract powder, adjusted to deliver 5 mg/mL to 20 mg/mL of marker flavonoids in Water for Injection, with pH adjusted to 6.0–7.5 using 0.1 M sodium hydroxide or hydrochloric acid. Compliance standards for this route include Ph. Eur. 2.9.9 for sub-visible particulate contamination, USP <788> for particulate matter in injections, VICH GL10 for impurity thresholds in new veterinary drug substances, and 21 CFR 211.113 for sterilisation process validation. Downstream production begins with dissolution at 35–40°C in a jacketed stainless steel vessel with bottom magnetic agitation; the solution is chilled to 20°C, clarified through 0.45 µm polyethersulfone capsules, then sterilised through 0.22 µm PVDF membrane filters in series. Filling into Type I borosilicate vials is conducted under unidirectional airflow with an area velocity of 0.45 m/s ± 20%, followed by terminal autoclaving at 121°C for 15 min if the marker compound stability data permit; thermolabile lots are aseptically filtered and sealed without terminal heat, but then the maximum bioburden before filtration must be ≤10 CFU/100 mL and the filter integrity bubble point tested before and after filling. Endotoxin limits are set at ≤0.5 EU/mL for mammalian parenteral products. The terminal presentation consists of 10 mL, 20 mL, 50 mL, and 100 mL multi-dose rubber-stoppered vials for intramuscular or subcutaneous administration in swine, cattle, and companion animals.

    Feed premix carrier selection and segregation thresholds

    The highest segregation risk is not at the final feed mill but during the first dilution of Houyanjing Powder into a carrier premix, because the extract particle density of 0.45–0.60 g/cm³ is substantially lower than corn meal particles, causing upward migration during pneumatic conveying. The formulation addition ratio for medicated premix ranges from 0.1 kg to 1.0 kg of API per 1000 kg final complete feed, but direct addition at this concentration is prohibited; a two-step geometric dilution is required, beginning at 1:10 with calcium carbonate of controlled particle size 180–250 µm, followed by a second 1:10 dilution onto wheat bran or rice husk carrier. Compliance obligations include 21 CFR 225 for medicated feed manufacturing, 21 CFR 558 registration for new animal drugs in feed, EU Regulation 1831/2003 for feed additive categories, ISO 22000:2018 food safety management, and GMP+ B2 for feed safety assurance. Production equipment is a horizontal ribbon mixer with a working volume of 1000 kg and a tip speed of 3–5 m/s; the mixer is filled to 60–70% of gross volume, and mixing time is validated by tracer studies to achieve a coefficient of variation ≤5% across 10 sampling points. Carrier moisture must be below 12% before addition, and 0.25% food-grade mineral oil is sprayed into the finished premix to reduce dust and electrostatic charge. This route yields 5 kg, 20 kg, and 25 kg multilayer paper bags with inner polyethylene liners, intended for incorporation into complete feed at the mill or as top-dress powders for swine and poultry farms; the premix form is selected where water medication is not feasible due to automatic nipple drinker clogging.

    Compression of Houyanjing Powder into companion animal tablets confronts a measurable plastic deformation limit because the extract contains residual polysaccharides that reduce powder flowability and increase hygroscopicity above 60% relative humidity; therefore the manufacturing process is configured around low-moisture wet granulation rather than direct compression. The formulation addition ratio is 5% w/w to 20% w/w of extract per tablet core, with a common 150 mg extract loading in a 750 mg tablet for dogs and a 50 mg extract loading in a 250 mg tablet for cats, the remainder consisting of microcrystalline cellulose, lactose monohydrate, crospovidone, and magnesium stearate. Compliance standards for this non-sterile oral tablet route include Ph. Eur. 2.9.8 resistance to crushing, Ph. Eur. 2.9.1 disintegration, USP <1217> tablet breaking force, USP <905> uniformity of dosage units, and VICH GL2 stability protocols for climatic zones III and IV. Downstream production is carried out in a high-shear granulator with impeller speed 300 rpm and chopper speed 1500 rpm, using purified water as binder at 10–15% w/w; wet granules are dried in a fluid-bed dryer at 55°C until loss on drying is 2.0–4.0%, then milled through a 1.0 mm screen. Compression is performed on a rotary tablet press with precompression force 5 kN and main compression force 8–18 kN, targeting tablet hardness of 30–70 N, friability ≤1.0%, and disintegration ≤15 min in 0.1 M hydrochloric acid at 37°C. Finished dosage forms include flat-faced scored tablets, chewable tablets with liver-based flavor coating, and film-coated tablets; the scored tablet format supports dose adjustment by body weight in companion animal veterinary practice.

    When direct-fill capsules replace granulated tablets for feline dosing

    Direct-fill capsule manufacturing for feline dosing avoids aqueous granulation but introduces a different constraint: the angle of repose of the milled extract–lubricant blend must remain below 35° to maintain die filling uniformity, and the API must be milled to D90 ≤ 100 µm to prevent demixing during the capsule filling cycle. The formulation addition ratio in capsules ranges from 10% w/w to 30% w/w of total fill weight, for example 125 mg extract in a size 1 capsule with total fill weight of 400 mg, using lactose monohydrate as the bulking diluent and magnesium stearate at 0.5% w/w as lubricant. Industry compliance standards applied to this dosage form include Ph. Eur. 2.9.5 uniformity of mass of single-dose preparations, Ph. Eur. 2.9.1 disintegration of capsules, USP <905> uniformity of dosage units, VICH GL1 analytical method validation, and 21 CFR 211.113 process validation for marketed veterinary products. Downstream processing uses a V-blender or bin blender at 25 rpm for 15 min, followed by an automatic capsule filling machine with dosator or tamping-pin stations operating at 30,000 capsules/hour; fill weight variability is controlled within ±3% and reject stations remove empty, split, and crushed capsules using capacitance and infrared sensors. Because the extract is hygroscopic, the filling room is maintained at 20–25°C and ≤40% relative humidity, and the capsules are packed in PVC/aluminium blisters with desiccant canisters immediately after metal detection. The manufactured capsule types include hard gelatin and hydroxypropyl methylcellulose capsules in 50 mg, 125 mg, and 250 mg extract strengths; the HPMC variant is specified for export to halal and vegetarian segments where porcine gelatin is unacceptable.

    Extrusion-spheronization of Houyanjing Powder into equine oral granules is selected only when the target dose exceeds the practical limit of a size 0 capsule, typically above 500 mg per administration, because the granular dosage form permits incorporation of palatability masking agents and controlled-release coatings without excessively increasing dose mass. The formulation addition ratio is 1% w/w to 5% w/w of extract in the final granule mass, with a representative composition of 2% w/w API, 55% w/w microcrystalline cellulose, 35% w/w lactose monohydrate, 3% w/w povidone binder, and 5% w/w sodium starch glycolate as disintegrant. Compliance standards include Ph. Eur. 2.9.10 sieve test for particle size distribution, Ph. Eur. 2.9.17 flowability, USP <786> analytical sieving, VICH GL2 stability testing, and ISO 3310-1:2016 test sieve specifications. The downstream process begins with dry blending in a planetary mixer, followed by wet granulation with purified water to a moisture content of 20–25%; the wet mass is extruded through a dome or radial screen extruder with 0.8–1.0 mm apertures and spheronized at 800–1200 rpm for 3–5 min until roundness exceeds 0.85. The spheres are dried in a fluid-bed dryer at 40°C to a final loss on drying ≤3.0%, sieved between 0.25 mm and 1.25 mm, and coated with a pH-dependent enteric polymer if the dose must bypass gastric degradation. The resulting presentations comprise 10 g, 25 g, and 100 g single-dose sachets, multi-dose tubs with calibrated scoops, and granules premeasured for mixing into pelleted feed for equine respiratory conditions; the granular route is specified when weight-based dosing for foals and adult horses requires fractional dose adjustment.

    Lyophilized cake collapse begins above the measured Tg' of the freeze-concentrated solution

    Freeze-dried injection powder containing Houyanjing extract requires mapping of the glass transition temperature of the maximally freeze-concentrated solution before the lyophilization cycle is fixed, because primary drying above Tg' causes cake collapse and higher residual moisture. The formulation addition ratio for lyophilized injection powder is expressed on a dry solids basis: the extract comprises 20% w/w to 60% w/w of total dry solids, with mannitol or glycine as the crystallizing bulking excipient at 40% w/w to 80% w/w; the pre-lyophilization liquid fill volume is 5 mL to 10 mL per vial with total solids of 5% w/v to 15% w/v. Compliance standards for this route include Ph. Eur. 5.1.1 for sterile preparation, EU GMP Annex 1 for aseptic processing, USP <922> water activity for lyophilized solids, VICH GL10 for degradation product limits, and 21 CFR 211.113 for process validation. Downstream manufacture consists of sterile filtration of the bulk solution through 0.22 µm PVDF filters into depyrogenated vials, followed by lyophilization with a shelf ramping cycle from −40°C to +30°C over 48 h; primary drying is executed at a shelf temperature of −20°C and chamber pressure of 0.1 mbar for 24 h, while secondary drying is performed at +30°C and 0.05 mbar for 6 h to reduce residual moisture below 2.0%. The cake appearance index is inspected for collapse, meltback, and shrinkage; vials with cracked or lifted cakes are rejected by machine vision. Finished parenteral forms include single-use vials containing 100 mg, 250 mg, and 500 mg of lyophilized extract, paired with diluent ampoules for reconstitution to 5 mL or 10 mL injection volume; this form is used where the marker compounds are not thermostable enough for terminal steam sterilisation.

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    Certification & Compliance
    More Introduction

    Houyanjing Powder Veterinary Grade Active Pharmaceutical Ingredient is supplied as a white to off-white crystalline powder for further manufacture into tablets, injections, capsules, powders, granules, premix, and solutions. Two standard grade codes are available: HYJ-P75 for solid oral, powder, granule, and premix applications, and HYJ-P25 for sterile solution and injection compounding after terminal sterilisation or aseptic processing. The numeric suffix in the code refers to the upper particle-size target by laser diffraction, Ph. Eur. 2.9.31: D90 ≤ 75 µm for HYJ-P75 and D90 ≤ 25 µm for HYJ-P25. The assay specification is 98.0–102.0% on the dried basis by HPLC with ultraviolet detection. Loss on drying is ≤ 0.5% when determined by Ph. Eur. 2.5.12; residue on ignition is ≤ 0.1% by Ph. Eur. 2.4.16; heavy metals are limited to ≤ 20 ppm by Ph. Eur. 2.4.8. Total related substances are controlled under VICH GL11, with total impurities ≤ 1.5% and any unspecified single impurity ≤ 0.10%. The material is not a finished veterinary medicinal product and is not labelled sterile. Where injection-grade material is specified, the bacterial endotoxin limit is < 0.025 EU/mg by Ph. Eur. 2.6.14, and total aerobic microbial count is ≤ 10 CFU/g by Ph. Eur. 2.6.12. The oral and premix grade carries a less stringent microbial limit of ≤ 100 CFU/g. These specification values are applied at batch release but should be reviewed against the manufacturer’s certificate of analysis, because compendial harmonisation status may vary by region and dosage form.

    Parameter HYJ-P75 HYJ-P25 Test Method
    Particle size D90 ≤ 75 µm ≤ 25 µm Ph. Eur. 2.9.31
    Bulk density 0.35–0.55 g/mL 0.25–0.45 g/mL Ph. Eur. 2.9.34
    Tapped density 0.50–0.70 g/mL 0.40–0.60 g/mL Ph. Eur. 2.9.34
    Loss on drying ≤ 0.5% ≤ 0.5% Ph. Eur. 2.5.12
    Residue on ignition ≤ 0.1% ≤ 0.1% Ph. Eur. 2.4.16
    Heavy metals ≤ 20 ppm ≤ 20 ppm Ph. Eur. 2.4.8
    Total related substances ≤ 1.5% ≤ 1.5% VICH GL11
    Bacterial endotoxin not specified < 0.025 EU/mg Ph. Eur. 2.6.14
    Total aerobic microbial count ≤ 100 CFU/g ≤ 10 CFU/g Ph. Eur. 2.6.12

    How Does the Injection-Grade Model Differ from Standard Oral-Grade Veterinary Powders?

    Sterile solution processing imposes different control boundaries than tablet granulation. A standard oral-grade veterinary API commonly has a single uncontrolled particle-size distribution, no bacterial endotoxin specification, and a total aerobic count limit that may be as high as 1000 CFU/g; it is unsuitable for parenteral compounding. The HYJ-P25 grade differs by adding dry heat depyrogenation at 250 °C for 45 min or equivalent, followed by air classification. HYJ-P75 is not merely an unprocessed precursor but is produced by a separate mechanical milling step at lower classifier speed, preserving hopper flowability while still controlling D90 ≤ 75 µm. This dual-grade approach avoids the common trade-off in which micronized powder improves content uniformity but retards powder discharge on high-speed tablet presses.

    For injectable preparations, the API is dissolved or suspended in Water for Injection, then filtered through a 0.22 µm PVDF or PES membrane. Filtration alone does not render a non-sterile API sterile. Terminal sterilisation or aseptic processing is required under 21 CFR 211 and EU GMP Annex 1. Sub-visible particulate matter in reconstituted solutions should comply with Ph. Eur. 2.9.19 limits, which specify not more than 6000 particles at ≥ 10 µm and not more than 600 particles at ≥ 25 µm per container. The bacterial endotoxin limit of < 0.025 EU/mg for HYJ-P25 is significantly lower than the 0.25 EU/mg level sometimes accepted for oral premix material. Users should confirm that the selected co-solvent system does not exceed VICH GL18 residual solvent limits. Published solubility data for this specific API in propylene glycol/water or ethanol/water blends is limited, so small-scale laboratory screening is required before scale-up. The key difference from a generic milled API is that HYJ-P25 is not simply jet-milled HYJ-P75; the two grades are manufactured with separate final classification and packaging procedures. Jet-milling can create amorphous surface domains that raise hygroscopicity and reduce chemical stability. The manufacturer controls milling gas pressure and classifier speed to limit the amorphous fraction as evaluated by dynamic vapour sorption. This reduces batch-to-batch variation in flow and compressibility compared with uncontrolled micronized powder.

    Granule and Premix Processing Boundaries, Including Flow and Segregation Data

    On a 300 L conical screw mixer, a 5 kg API charge blended with 50 kg microcrystalline cellulose-lactose premix at 12 rpm for 15 min produced blend uniformity RSD ≤ 3.0% for HYJ-P75. The same trial with HYJ-P25 showed electrostatic adhesion to stainless steel when relative humidity fell below 30%, requiring addition of 0.5% w/w colloidal silicon dioxide and room humidity control at 40–60%. These observations come from pilot-scale mixing and should not replace site-specific blend validation. For dry granulation, roller compaction at roll pressure 4–8 MPa, gap 1.0–1.5 mm, and milling screen 0.5–1.0 mm produced granules with Carr’s index ≤ 25% and Hausner ratio ≤ 1.25 when tested by Ph. Eur. 2.9.36. Tablet compression on a 16-station B-tool rotary press at compression force 8–12 kN gave friability < 1.0% by USP 1216. Published data for Houyanjing API in this specific configuration is limited; the above ranges are derived from analogous low-solubility veterinary APIs and should be revalidated for each batch and formulation.

    For wet granulation, aqueous binder can be used only if the granule is dried to LOD ≤ 0.8% before compression; otherwise sticking and picking are observed on the lower punch face. Strong oxidising agents should be avoided unless a forced degradation study confirms chemical compatibility. The material should not be co-milled with amine-based additives without prior compatibility testing, because amine functional groups can accelerate degradation of structurally similar heterocyclic actives through nucleophilic attack. This is not an established cross-linking mechanism for Houyanjing API but a conservative processing boundary based on functional group susceptibility. In premix operations, carrier particle size should be within 100 µm of the API grade to reduce percolation segregation during transfer and bag filling. A two-stage dilution is recommended: first prepare a 1:100 intermediate premix, then dilute to 1:1000 final feed premix. Geometric dilution should be used because direct addition of concentrated API to a large carrier mass can produce ordered-unit segregation and poor assay uniformity in the final feed.

    When the API Is Co-Milled with Acidic Excipients or Held at High Relative Humidity

    Moisture uptake increases at relative humidity above 60%. The powder should be pre-dried at 50–60 °C for 2–4 h in a tray dryer if LOD exceeds 0.8% before encapsulation or direct compression. Storage in HDPE drums with heat-sealed foil liners and desiccant is specified below 25 °C and 60% RH. When co-milled with acidic excipients such as citric acid or malic acid, the dry powder blend may become sticky due to the amorphous surface fraction generated by milling. This is a physical incompatibility and not necessarily chemical degradation. A forced degradation screen with 0.1 M HCl, 0.1 M NaOH, and 3% H₂O₂ for 24 h is recommended to establish degradation products before selecting a granulation binder or solution vehicle. For oral solutions, the API should be dissolved or suspended in a buffered vehicle, and the pH should be maintained within 4.0–6.5 unless solubility data support a wider range.

    For sachet powders and oral granules, the API is dry-mixed with dextrose or lactose carrier in stepwise geometric dilution. Capsules may be filled on dosator-type or tamping-pin capsule machines; dosing weight variation is controlled by ensuring powder bed depth remains constant and relative humidity is maintained at 40–60%. Solution dosage forms must meet VICH GL18 residual solvent class limits. Ethanol and propylene glycol are common class 3 solvents, but published solubility data for this specific API is limited. The injection-grade model should be subjected to sterility assurance validation after aseptic filling or terminal heat sterilisation; the API itself is not supplied sterile. When no occupational exposure limit is published for the active substance, a default control banding approach based on COSHH Essentials should be applied during weighing, milling, and packing until a site-specific toxicological review establishes a formal exposure limit. All processing areas should use local exhaust ventilation and dust extraction because the fine-particle grade HYJ-P25 generates measurable airborne dust during open transfer.

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