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

    • Product Name: Zhizhuxiang Capsules 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 628428
    Product Name Zhizhuxiang Capsules Veterinary Grade API
    Alternative Name Zhizhuxiang Extract
    Chinese Name 蜘蛛香提取物
    Plant Source Valeriana jatamansi Jones
    Part Used Rhizome and Root
    Product Type Veterinary Grade Active Pharmaceutical Ingredient
    Grade Veterinary Grade
    Appearance Brown to dark brown fine powder
    Color Brown to dark brown
    Odor Characteristic, slightly aromatic
    Taste Bitter, slightly sweet
    Solubility Partially soluble in water, soluble in ethanol
    Purity ≥98% (HPLC)
    Moisture Content ≤5.0%
    Ash Content ≤5.0%
    Heavy Metals ≤10 ppm
    Arsenic ≤2 ppm
    Lead ≤3 ppm
    Mercury ≤0.1 ppm
    Total Plate Count ≤1000 CFU/g
    Yeast And Mold ≤100 CFU/g
    Particle Size 80-100 mesh
    Dosage Forms Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions
    Target Species Livestock, poultry, aquaculture
    Administration Route Oral, injection (as formulated)
    Storage Condition Cool, dry, ventilated place, away from light
    Shelf Life 24 months
    Packaging 25 kg fiber drum with double plastic bags inside
    Quality Standard Enterprise Standard
    Certification GMP, ISO9001, HACCP
    Origin China

    As an accredited Zhizhuxiang Capsules 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 Zhizhuxiang Capsules Veterinary Grade API is supplied in sealed, moisture-resistant foil-lined fiber drums, 25 kg net each, labeled with batch/expiry.
    Container Loading (20′ FCL) 20′ FCL loading: securely palletized, labeled Zhizhuxiang Capsules Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions; clean, dry container.
    Shipping Zhizhuxiang Capsules Veterinary Grade API is shipped worldwide in sealed, tamper-evident, moisture-barrier packaging, labeled per IATA/IMDG/ADR regulations. Each shipment includes SDS, COA, and customs documents, with temperature control and tracking available. Handling follows GMP and chain-of-custody requirements to preserve potency and safety. Secure, compliant logistics ensure timely delivery to approved destinations.
    Storage Store Zhizhuxiang Capsules Veterinary Grade API in original, tightly sealed, labeled containers in a cool, dry, well-ventilated place. Protect from light, moisture, heat, and contamination. Keep away from food, feed, children, and incompatible materials. Maintain manufacturer-recommended temperature and humidity. For tablets, injections, capsules, powders, granules, premix, or solutions, follow product-specific stability, expiry, and local veterinary regulations.
    Shelf Life For veterinary-grade Zhizhuxiang Capsules API, shelf life is typically 24 months under sealed, cool, dry, dark storage; confirm via COA/SDS.
    Application of Zhizhuxiang Capsules Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    The Zhizhuxiang capsule-derived veterinary-grade API is supplied as a hygroscopic, multicomponent botanical extract containing alcohol-insoluble polysaccharides, sesquiterpene lactones, and methoxyflavonoid aglycones. Processing decisions for finished dosage forms are controlled by two measurable raw-material attributes: apparent viscosity of a 10% w/v aqueous dispersion and loss on drying after 24 h at 60% RH. The following application routes are separated by equipment-specific constraints rather than by animal species, because the powder’s mechanical and rheological behaviour changes with water activity and moisture exposure. The routes described below include tablet manufacture, parenteral solution processing, hard capsule filling, medicated premix production, oral solution formulation, and moisture-sensitive oral powder or granule packaging.

    In wet-granulated veterinary tablet manufacture, the main process constraint is the water-binding behaviour of the extract rather than its mixing compatibility with standard fillers. The extract is incorporated at 4.0–10.0% w/w of the final tablet core blend. The compliance framework for such tablets includes uniformity of dosage units under Ph. Eur. 2.9.40, disintegration under Ph. Eur. 2.9.1, and dissolution testing for immediate-release formulations under Ph. Eur. 2.9.3, with residual solvent limits from VICH GL18 applied to the extraction-solvent profile. Production on a 300 L high-shear granulator begins with dry blending of the extract with microcrystalline cellulose and pregelatinised starch for 5 min at 200 rpm impeller speed, followed by aqueous binder addition at 12–18% w/w. The extract’s pectic fraction binds water heterogeneously; when the same water mass is used across batches, torque on an instrumented high-shear granulator can rise from 18–22 N·m to 34–40 N·m, forcing a real-time reduction in binder liquid of 3–5% to keep granule size between 125 µm and 800 µm. Wet mass is milled through a 1.2 mm screen, dried in a fluid-bed dryer to a final moisture of 2.5% or less, dry-milled, and lubricated with magnesium stearate at 0.5–1.0% w/w before rotary compression. Tablets compressed to 8–14 kp hardness and friability below 1.0% are the terminal product; if friability exceeds 1.0% at hardness above 14 kp, film coating may hide edge erosion but does not correct an overdried or over-lubricated core.

    Why Does Terminal Sterilisation of Aqueous Zhizhuxiang Extract Fail Above pH 4.5?

    Injectable solutions containing the standardised extract must be formulated on the acidic side of the extract’s methoxyflavonoid aglycone solubility boundary, because neutral or weakly alkaline conditions precipitate flavonoid aglycones and produce visible particulate after autoclave cooling. The addition ratio is limited to 0.1–1.5 mg/mL of extract solids in the final solution; published data for injection-specific exposure of this botanical multicomponent mixture is limited, so terminal sterilisation validation must be supported by species-specific osmolality, endotoxin, and particulate controls rather than by read-across from oral routes. Compliance follows Ph. Eur. 2.6.1 for sterility, Ph. Eur. 2.9.19 for sub-visible particulate contamination, Ph. Eur. 2.9.17 for extractable volume, and cleanroom classification requirements of EU GMP Annex 1: 2022-08-25, with grade A filling under ISO 5 conditions. Production begins by dispersing extract solids in Water for Injection at 35–40°C with pH adjusted to 3.8–4.2 using a citric acid buffer system. The solution is circulated through activated carbon for 20 min, prefiltered through a 1.2 µm glass-fibre depth filter, passed through a 0.45 µm PVDF membrane, and sterile-filtered through a 0.22 µm PVDF capsule immediately before filling. Terminal sterilisation is performed at 121°C for 15 min, but only after bench-scale pH-stability screening confirms that filter-blocking flocculation does not occur during cooling. The terminal product is a clear aqueous injection solution in vials or multi-dose containers for parenteral veterinary administration; buffering above pH 4.5 is contraindicated because the autoclavable drug product may fail visual inspection and sub-visible particle counts under Ph. Eur. 2.9.19.

    Hard capsule filling of the standardised extract is a dry-blend operation rather than a granulation process, because the powder remains flowable when conditioned at low humidity and because thermal history above 55°C is unnecessary for capsule manufacture. The extract is incorporated at 20.0–40.0% w/w of fill mass in size 1 HPMC or hard gelatin capsules, with fumed silica at 1.0–2.0% w/w to control flow; compliance follows Ph. Eur. 2.9.40 for content uniformity and Ph. Eur. 2.9.1 for disintegration, while the filling room is held below 40% RH to prevent shell softening and hopper sticking.

    Premix Segregation Is Controlled by Angle-of-Repose Match, Not Only Blend Time

    Before the extract is introduced into vitamin-mineral premixes, it is adsorbed onto a particulate carrier because the neat botanical powder has an angle of repose near 45° and separates rapidly from granular feed matrices. The addition ratio in the intermediate premix is 2.0–10.0% w/w of extract solids, with final feed inclusion rates typically between 0.5 kg and 5.0 kg premix per tonne of complete feed depending on species and target dose. Compliance is based on medicated feed cGMP requirements under 21 CFR 225.1, the EU medicated feed rules in Regulation (EU) 2019/4, and homogeneity evaluation under Ph. Eur. 2.9.40 as adapted for multi-unit dry powders; carry-over limits and cleaning validation are handled under site-specific feed safety programmes. Production begins by adsorbing the extract onto precipitated silica or calcium carbonate carrier in a paddle mixer at 30–50 rpm for 15 min, then diluting in a ribbon blender until the coefficient of variation for a marker compound is below 10%. Segregation is minimised by matching the angle of repose between the loaded carrier and the feed base rather than by extending blend time, which does not correct electrostatic fines migration or flow sorting. The terminal products are veterinary premix bags and final medicated mash or pelleted feed; pellet die temperatures above 75°C are avoided because the extract’s terpenoid lactones show measurable thermal degradation above this threshold.

    Oral Solution Co-solvent Limits for High-Loading Veterinary Drenches

    In oral drench and drinking-water solution manufacturing, the limiting variable is the extract’s cold-water dispersibility, which is poor below 35°C because the dehydrated pectic fraction hydrates slowly and forms gel-like lumps. The addition ratio is 0.2–2.0% w/v extract solids in final solution; above 2.0% w/v, a co-solvent system of propylene glycol or glycerol at 5–15% v/v is required to maintain clarity, while above 5.0% w/v the solution may become thixotropic and difficult to transfer through filling lines. Compliance follows Ph. Eur. 2.9.17 for extractable volume, Ph. Eur. 2.9.3 for dispersion behaviour where appropriate, and preservative effectiveness under Ph. Eur. 5.1.3; cleanability limits are set by CIP validation using riboflavin tests in the filling circuit. Production uses a heated stainless-steel tank at 40°C with high-shear recirculation through a 75 µm basket strainer, followed by cooling to 20–25°C before volumetric filling into amber HDPE bottles with child-resistant caps for drench use or into larger HDPE drums for drinking-water proportioner systems. A nitrogen purge is applied during storage if oxygen-sensitive fractions are retained at these loading levels. The terminal product is a preserved oral solution or drench for individual animal administration or water-mediated delivery.

    When Moisture Vapour Transmission Rate Exceeds 0.5 g/m²/24 h in Sachet Granules

    When the extract is processed into moisture-barrier sachet granules or oral powders, the failure point on stability is not chemical degradation but moisture ingress through the package structure, which raises the extract’s glass transition and converts free-flowing granules into agglomerated masses. The addition ratio is 10.0–25.0% w/w extract solids in the granule formulation, with moisture content of the finished granules held below 3.0% by Karl Fischer titration. Compliance is based on Ph. Eur. 2.9.36 for powder flow, Ph. Eur. 2.9.7 for particle-size distribution, and stability testing under ICH Q1A(R2) conditions, with aluminium foil sachets selected to provide a moisture vapour transmission rate below 0.5 g/m²/24 h at 38°C/90% RH. Production uses roller compaction or fluid-bed spray granulation with an aqueous binder; granules are sieved to 150–850 µm, and the 150 µm fines fraction is limited to below 30% because fines segregate during sachet filling and increase dust exposure. The terminal product is a unit-dose or multi-dose sachet of oral powder or granules for direct administration or reconstitution in drinking water; packaging in pure LDPE film is inadequate at these loadings because moisture ingress can exceed the 3.0% moisture limit within 30 days under zone IVb conditions.

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    Certification & Compliance
    More Introduction

    Zhizhuxiang Capsules Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is released as a multi-route active pharmaceutical ingredient whose grade designation is tied to the intended dosage form rather than to a single pharmacopoeial monograph identity. The model code is the manufacturer’s veterinary-grade identifier; no international nonproprietary name or compendial monograph currently assigns the trade name to a single chemical entity, and therefore the certificate of analysis remains the controlling document for batch-specific assay, related substances, residual solvent, and elemental impurity profiles. Material intended for solid oral dosage forms is released under non-sterile requirements consistent with Ph. Eur. 5.1.4, while injectable and solution routes require additional endotoxin, sterility, and sub-visible particulate controls consistent with Ph. Eur. 2.6.14, Ph. Eur. 5.1.1, and USP ⟨788⟩. Specification layers include identity by infrared or chromatographic retention, assay by high-performance liquid chromatography, related substances by gradient HPLC, residual solvents by headspace gas chromatography, elemental impurities by inductively coupled plasma-mass spectrometry, water content by Karl Fischer titration, and particle size distribution by laser diffraction. Each dosage form imposes a distinct release profile: tablet and capsule grades emphasize flow, compressibility, and dissolution; premix grades emphasize dilution homogeneity and segregation resistance; injection grades emphasize endotoxin burden, particulate load, osmotic compatibility, and sterility.

    What separates injectable-grade Zhizhuxiang API from oral premix-grade material?

    Injectable-grade material cannot be generated by repackaging feed-grade or oral-grade powder. The bacterial endotoxin acceptance criterion is derived from the maximum bolus dose and route of administration under USP ⟨85⟩, using the relationship E = K/M, where K is 5 EU/kg for intravenous administration and M is the maximum dose in mg per kg of body weight per hour. For an illustrative intravenous dose of 10 mg/kg/h, the resulting API endotoxin limit is ≤0.5 EU/mg; lower doses or intrathecal routes can drive the limit below 0.1 EU/mg. Injectable-grade material must also pass sterility testing by direct inoculation or membrane filtration according to Ph. Eur. 5.1.1, and sub-visible particulate matter is controlled by light obscuration with acceptance values for containers under USP ⟨788⟩ of ≥10 µm: ≤6000 per container and ≥25 µm: ≤600 per container. Oral premix-grade material, by contrast, is non-sterile and is released only when total aerobic microbial count does not exceed 100 CFU/g, total combined yeasts and moulds does not exceed 10 CFU/g, and bile-tolerant gram-negative bacteria are absent in 1 g under Ph. Eur. 5.1.4. The route-specific difference also changes processing: injectable-grade API requires depyrogenated containers, dedicated air handling, and terminal filtration through 0.22 µm membranes, whereas oral premix-grade material is dispersed into feed carriers under standard dry blending conditions.

    For tablet and capsule processing, the API is dry-blended in a bin blender with an intensifier bar at 10–15 rpm until blend uniformity meets Ph. Eur. 2.9.40 acceptance values. Wet granulation in a high-shear mixer requires purified water addition until impeller torque reaches 40–60% of motor load; granulates are dried in a fluid-bed dryer with inlet air 55–65°C to loss-on-drying ≤2.0%. Milling through a conical mill with 0.8 mm screen provides granules with D50 200–400 µm. Tablets are compressed on a rotary press with precompression force 5–10 kN and main compression 20–35 kN; hardness target is 70–120 N depending on dissolution response. Capsule filling with a dosator or tamping-pin machine requires tapped density 0.45–0.70 g/mL and Carr index ≤25 for consistent fill weight. For powders intended for direct use, the particle size distribution is measured by laser diffraction under ISO 13320; a D90 below 250 µm is normally targeted when the product is combined into a 1:100 or higher dilution premix to reduce segregation. These processing windows are representative for medium-density botanical or synthetic veterinary APIs; published data for the specific Zhizhuxiang trade-name configuration are limited, and development-scale confirmation against the manufacturer’s CoA is required before transfer to production equipment.

    Solubility, pH, and solution stability place measurable constraints on formulation

    Solution and injection use requires characterization of aqueous solubility across pH 2.0–8.0 at 20–25°C. Potentiometric pH is measured according to Ph. Eur. 2.2.3, and osmolality is measured according to Ph. Eur. 2.2.35. For multidose or single-dose preparations, the API is dissolved initially in a portion of water for injection with agitation at 200–500 rpm; pH is corrected with 0.1 M hydrochloric acid or 0.1 M sodium hydroxide to a target range of pH 4.5–6.5 unless forced degradation data justify an alternative. If terminal steam sterilization at 121°C for 15 min is used, the cycle must be validated by sterility testing under Ph. Eur. 5.1.1 and supported by assay and related substance data showing no degradation outside the release specification. When terminal sterilization is not feasible because of heat lability, aseptic filtration through a 0.22 µm polyethersulfone filter is performed into depyrogenated vials, followed by sterility and sub-visible particulate testing under Ph. Eur. 2.9.19 and USP ⟨788⟩. Multidose solutions containing no preservative are limited by the absence of antimicrobial efficacy; where preservative is present, the formulation must meet the acceptance criteria of Ph. Eur. 5.1.3 for antimicrobial preservation. The difference from solid oral forms is that solution stability is controlled by first-order degradation kinetics and pH-dependent hydrolysis rather than by moisture sorption and tablet hardness.

    Residual solvent and elemental impurity control points

    Residual solvent testing follows headspace gas chromatography with flame ionization detection or mass spectrometry, and limits are selected according to ICH Q3C(R8) and the veterinary Guideline VICH GL18(R2). Class 1 solvents are controlled at parts-per-million levels; Class 2 solvents are controlled at the permitted daily exposure converted to concentration limits by the product’s maximum daily dose. Elemental impurity control is aligned with ICH Q3D and the veterinary equivalent VICH GL30, with route-specific limits for As, Cd, Hg, and Pb applied by inductively coupled plasma-mass spectrometry. The following representative Class 1 and Class 2 limits are compendial default values and do not replace product-specific CoA limits.

    Representative residual solvent limits per ICH Q3C(R8) and VICH GL18(R2)
    SolventClassConcentration limit
    BenzeneClass 12 ppm
    Carbon tetrachlorideClass 14 ppm
    1,2-DichloroethaneClass 15 ppm
    ChloroformClass 260 ppm
    MethanolClass 23000 ppm
    TolueneClass 2890 ppm

    Differences from other products are most visible in the grade comparison matrix. A technical-grade material may have assay, impurity, solvent, and residue profiles that are not suitable for therapeutic administration; a veterinary oral/premix grade must meet non-sterile microbial and solvent limits but is not required to be sterile; a veterinary injectable grade must meet endotoxin, sterility, particulate, and osmolality controls. Human-grade API is produced under ICH Q7 and often under dedicated line changeover controls, but it may lack food-producing species residue depletion and withdrawal period documentation required under Regulation (EU) No 37/2010 and Regulation (EU) 2019/6. The Zhizhuxiang veterinary-grade designation is therefore not simply a purity label; it indicates that the batch is accompanied by route-specific documentation, stability data, and contamination controls suitable for veterinary pharmaceutical formulation.

    Grade-dependent release criteria for multi-route veterinary use
    AttributeTechnical gradeOral/premix gradeInjectable grade
    AssayNot standardizedPer manufacturer CoA, commonly 95.0–105.0%Per route validation, commonly 95.0–105.0%
    Bacterial endotoxinNot testedNot required for non-sterile oral≤0.5 EU/mg or K/M-derived limit per USP ⟨85⟩
    SterilityNot testedNot requiredMeets Ph. Eur. 5.1.1
    Microbial qualityVariableTAMC ≤100 CFU/g per Ph. Eur. 5.1.4Sterile
    Sub-visible particlesNot controlledNot controlled≥10 µm: ≤6000; ≥25 µm: ≤600 per container per USP ⟨788⟩
    Residual solventsUnknownMeets VICH GL18(R2)Meets VICH GL18(R2)
    Elemental impuritiesUnknownMeets VICH GL30Meets VICH GL30

    When formulation into premix approaches a 1:100 dilution ratio, segregation risk dominates process capability

    Premix and granule dilution requires assessment of particle size mismatch, density difference, and electrostatic charge. If the API has D50 50–150 µm and the feed carrier has D50 300–800 µm, dry blending in a ribbon blender at 20–40 rpm can achieve homogeneity but the mixture is sensitive to segregation during discharge and transport. Sampling under ISO 2859-1 or an equivalent acceptance sampling plan is used to verify that active content remains within ±10% of the labeled claim across 10 sampled points. Segregation is reduced by matching carrier particle size distribution, adding binder such as 2–5% povidone or starch paste during wet granulation, and controlling residual moisture to ≤5.0%. For powder and premix operations without granulation, the API should be pre-blended with a small portion of carrier at 1:3 before addition to the full batch; this staged dilution is evaluated by blend uniformity testing under Ph. Eur. 2.9.40. Equipment-specific failure modes include dead zones at the base of vertical mixers, and electrostatic coating of the conveyor if relative humidity falls below 30%; when ambient RH is below 30%, grounding of the blender and controlled humidification to 40–45% RH reduce charge accumulation. The difference from tablet and capsule formulations is that premix does not benefit from unit-dose metal detection or individual hardness testing, so the entire batch must remain uniform under practical field handling conditions.

    Storage stability is controlled under long-term conditions of 25°C/60% RH and accelerated conditions of 40°C/75% RH according to VICH GL3 and ICH Q1A(R2) principles. Packaging must provide a moisture barrier; aluminum foil pouches, PVDC-coated blisters, or HDPE drums with desiccant are selected based on moisture vapor transmission rate. At relative humidity above 60%, powders and granules should be pre-dried before tableting or capsule filling to avoid picking, sticking, and poor flow. The product should not be mixed with amine-based additives when solution stability data show risk of Schiff-base formation or premature degradation; compatibility studies using binary mixtures stored at 40°C/75% RH for 4 weeks are required before any new excipient is introduced. For injections and solutions, the API solution should be protected from light when photodegradation data show a measurable increase in related substances after 24 h under ICH Q1B light conditions. The operational boundary is therefore defined not by a single storage temperature but by the dosage form, packaging, and the validated retest period in the manufacturer’s stability summary.

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