| HS Code | 234360 |
| Product Name | Triclobisonium Veterinary Grade API |
| Api Name | Triclobisonium |
| Chemical Name | Triclobisonium chloride |
| Cas Number | 154-68-7 |
| Grade | Veterinary Grade |
| Product Category | Veterinary Active Pharmaceutical Ingredient |
| Therapeutic Category | Antiseptic and disinfectant |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Veterinary Use | Treatment and prevention of bacterial infections in animals |
| Target Species | Cattle, swine, poultry, sheep, goats, dogs, cats |
| Administration Route | Oral, topical, injectable |
| Appearance | White to off-white crystalline powder |
| Solubility | Soluble in water and alcohol |
| Purity | ≥99.0% |
| Storage Conditions | Store in a cool, dry, well-ventilated place away from direct sunlight |
| Shelf Life | 24 months |
| Packaging | 25 kg fiber drum, 1 kg aluminum foil bag |
| Regulatory Status | Veterinary prescription only |
As an accredited Triclobisonium 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 | Triclobisonium Veterinary Grade API packed in 25 kg double-lined fiber drums, sealed for tablets, injections, capsules, powders, granules, premix, solutions. |
| Container Loading (20′ FCL) | 20′ FCL loading: palletized drums of Triclobisonium Veterinary Grade API, suitable for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Triclobisonium Veterinary Grade API for tablets, injections, capsules, powders, granules, premixes, and solutions is shipped in sealed, light-resistant, moisture-proof containers under supplier-specified conditions. Each shipment includes COA, SDS, and batch documentation. Packages are labeled and handled according to applicable transport and veterinary chemical regulations. |
| Storage | Store Triclobisonium Veterinary Grade API in tightly closed, original containers in a cool, dry, well-ventilated area, protected from light, moisture, heat, and contamination. Keep separate from food, feed, and incompatible chemicals. Maintain controlled access, clear labeling, and inventory records. For tablets, injections, capsules, powders, granules, premix, or solutions, follow manufacturer and pharmacopoeial storage conditions and expiry requirements. |
| Shelf Life | Shelf life varies by dosage form; typically 24–36 months when stored sealed, dry, protected from light, per manufacturer stability data. |
In Type A medicated article and Type B medicated feed premix manufacturing, triclobisonium veterinary grade API is first normalized for particle size before it enters a carrier-based dilution line. The dry blending step is constrained by the API’s particle-size distribution, which should be controlled to a D50 of 75–150 µm and a D90 of ≤355 µm when the intended carrier is lactose monohydrate or solvent-extracted soybean meal. Industry compliance for this sector is anchored to 21 CFR 225 current good manufacturing practice for medicated feed, 21 CFR 558 new animal drugs for use in animal feed, and the batch-release provisions of the marketing authorisation under Regulation (EU) 2019/6. Uniformity is assessed by sampling at the beginning, middle, and end of mixer discharge; coefficients of variation at ≤5.0% across ten consecutive samples are required for batch release, while carryover limits for non-target feed lines are set at ≤1.0% of the lowest labeled concentration unless the registration specifies a stricter threshold. A typical formulation addition ratio is a triclobisonium premix intermediate at 2.0–10.0% w/w active, subsequently incorporated into complete feed at 0.5–5.0 kg per metric tonne, equivalent to 10–500 g active per tonne depending on the approved species and indication. The downstream production process uses a horizontal ribbon mixer or paddle mixer with a working volume of 50–80% capacity; the API is pre-blended in a geometric dilution sequence with 1–5 kg of carrier before introduction into the main batch. When granulation is specified, low-shear wet granulation with purified water at ≤25% w/w water addition is followed by fluidised-bed drying at inlet air temperature 60–70 °C and final screen milling through 0.8 mm mesh. Terminal finished product types include Type A medicated articles for further dilution, Type B medicated feed premixes for farm mixing, and Type C complete feeds for swine or poultry. Batch records for such premixes require moisture content ≤5.0% and total plate count below the limit stated in the marketing authorisation. Avoid alkaline carriers that raise the microenvironment pH above 8.0 unless pre-blend stability data support the interaction.
| Premix carrier | Bulk density | Moisture limitation | Active premix addition ratio |
|---|---|---|---|
| Lactose monohydrate | 0.55–0.70 g/cm³ | ≤1.0% | 2.0–5.0% w/w |
| Solvent-extracted soybean meal | 0.55–0.65 g/cm³ | ≤10.0% | 5.0–10.0% w/w |
| Ground limestone | 1.00–1.30 g/cm³ | ≤0.5% | Not recommended unless coated for pH-sensitive formulations |
The controlling variables for oral solutions and water-soluble powders intended for automatic proportioner delivery are pH, water hardness, and stock solution hold time. Compliance is anchored to 21 CFR 558 when the drinking water line is linked to medicated feed regulation, Regulation (EU) 2019/6 for veterinary medicinal products, and Ph. Eur. 2.9.40 for uniformity of dosage units when the formulation is packaged as a single-dose powder. The formulation addition ratio for a stock solution is commonly prepared at 0.5–5.0% w/v active, then proportioned at 1:128 or 1:200 through a metering pump to yield an in-use concentration of 0.005–0.05% w/v active. Hard water above 200 ppm CaCO₃ can reduce clarity if the API is formulated as a chloride salt; therefore purified water or softened water is specified in the compounding record. The downstream production process for water-soluble granules begins with blending the API with buffering salts and maltodextrin in a high-shear mixer, followed by moisture-activated granulation and drying to residual moisture ≤3.0%. The dried granules are milled and screened to 0.315–0.500 mm before filling into laminated foil sachets under ≤30% RH. For liquid solutions, the manufacturing process includes dissolving the API in water for oral use at 20–25 °C, adding a preservative system where the registration permits, filtering through 10 µm polypropylene depth media, and filling into opaque HDPE containers. Terminal finished product types include oral solution in 1 L and 5 L high-density polyethylene containers, powder sachets for direct addition to stock tanks, and bulk liquid concentrates for proportioner injection. Avoid free chlorine residuals above 4 ppm unless a reducing stabilizer is included in the formulation.
Terminally sterilised injectable solutions containing triclobisonium require process validation across load configuration, container size, and worst-case fill volume. Compliance is tested against EU GMP Annex 1 (2022), 21 CFR 210 and 21 CFR 211 for current good manufacturing practice in finished pharmaceuticals, Ph. Eur. 2.6.1 sterility, and Ph. Eur. 2.6.14 bacterial endotoxins. The formulation addition ratio places the active at 0.5–5.0% w/v in an aqueous isotonic vehicle, with sodium chloride adjusted to 0.85–0.90% w/v and pH between 5.5 and 6.5 if solution stability data support. The downstream production process uses a closed stainless-steel mixing vessel equipped with a bottom-mounted magnetic stirrer; the solution is filtered through 0.45 µm then 0.22 µm polyethersulfone membranes before filling under Grade A unidirectional airflow. Terminal sterilisation at 121 °C for 15 min is used when the active demonstrates no more than 2.0% assay loss and no degradation product above the identification threshold; otherwise, aseptic filtration with post-fill integrity testing by forward-flow bubble point is applied. Terminal finished product types include 50 mL and 100 mL glass vials sealed with chlorobutyl rubber stoppers, with residual oxygen controlled by nitrogen overlay below 5.0% headspace oxygen.
| Test parameter | Standard / method | Release criterion |
|---|---|---|
| Appearance | Visual inspection | Clear, colorless to pale yellow solution |
| Assay | Ph. Eur. 2.2.29 validated HPLC | 95.0–105.0% of label claim |
| Bacterial endotoxins | Ph. Eur. 2.6.14 | <0.50 EU/mg |
| Sterility | Ph. Eur. 2.6.1 | No growth after 14 days |
| Particulate matter ≥10 µm | Ph. Eur. 2.9.19 | ≤6000 particles per container |
| Particulate matter ≥25 µm | Ph. Eur. 2.9.19 | ≤600 particles per container |
Wet granulation of triclobisonium tablets for companion animal and swine administration is specified when the API bulk density falls below 0.35 g/cm³ and direct compression produces unacceptable weight variation. Industry compliance for this solid-dose sector follows 21 CFR 211 finished pharmaceutical GMP, Ph. Eur. 2.9.5 uniformity of mass, Ph. Eur. 2.9.8 resistance to crushing, and Ph. Eur. 2.9.3 dissolution; dissolution Q-value is typically set at ≥75% in 45 min for the reference product unless the marketing authorisation varies. The formulation addition ratio for tablet cores is 5–25% w/w active, with per-unit content determined by the approved species dose; common commercial core masses range from 80 mg to 1,200 mg, with active content ranging from 10 mg to 250 mg per tablet. The downstream production process uses a high-shear granulator with impeller speed 200–400 rpm, purified water or an aqueous binder solution at 8–15% w/w, and fluidised-bed drying to final moisture 2.0–4.0%; dried granules are screened through 0.9 mm sieve before blending with disintegrant and lubricant. Compression is carried out on a rotary tablet press with punch tip diameter 8–13 mm, pre-compression force 3–5 kN, main compression force 7–15 kN, and press speed 150,000–250,000 tablets/h. Capsule filling for powder blends uses an automatic capsule filler with dosator or tamping-pin technology, targeting weight variation below ±3.0%. Terminal finished product types include chewable tablets, film-coated tablets, and hard gelatin capsules packaged in PVC/aluminium blisters or HDPE bottles with induction-sealed closures. Pre-drying of API and excipients is required when ambient relative humidity exceeds 60%; avoid magnesium stearate levels above 1.0% w/w unless an extended disintegration study supports the formulation.
For neonatal calves and lambs, triclobisonium granulated oral powders are dispersed in milk replacer or water and administered through nipple feeders or dosing pumps. Regulatory compliance references VICH GL18 for residual solvents, Regulation (EU) 2019/6 for veterinary medicinal products, and 21 CFR 210 and 21 CFR 211 where equipment cleaning validation is shared across species. The formulation addition ratio for the oral granule is 2.0–10.0% w/w active in a lactose or glucose carrier, diluted at point of use to 0.1–1.0 g active per litre of reconstituted liquid. The downstream production process is lower-shear than the tablet granulation route: the API is blended with carrier, granulated in a fluid-bed granulator with inlet air temperature 50–60 °C, spray rate 150–250 mL/min, and final sieve cut through 0.5 mm mesh. Granules are filled into single-dose 10 g or 20 g sachets under low-humidity conditions (≤30% RH) to prevent caking. Terminal finished product types include sachet granulated oral powders, bulk jars for automated calf feeders, and paste formulations where a non-aqueous carrier is added in a planetary mixer. Avoid reconstitution with water above 40 °C unless the formulation dossier includes thermal degradation data. Published multi-batch stability data across all neonatal dosing trough materials are limited; compatibility with polyurethane nipple liners and stainless-steel dosing equipment should be confirmed under field conditions before assigning in-use dating.
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Triclobisonium Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is supplied as triclobisonium chloride, a cationic bis-quaternary ammonium salt. The active moiety contains two quaternary nitrogen centres separated by an aliphatic spacer, with long-chain alkyl substituents on the terminal nitrogens. This dimeric structure distinguishes the compound from single-centre quaternary ammonium agents such as benzalkonium chloride, particularly in charge density, adsorption behaviour on negatively charged surfaces, and complexation with anionic excipients. The API is manufactured in two physical grades: a non-sterile milled grade for solid oral and in-feed preparations, and a sterile crystallized grade for parenteral compounding. The non-sterile grade is a white to off-white crystalline powder with high aqueous solubility and hygroscopic behaviour. The product is not an anthelmintic and is not to be confused with triclabendazole, which has a similar nonproprietary stem but belongs to a different chemical and pharmacological class.
In the absence of a harmonised monograph in the current European Pharmacopoeia or United States Pharmacopeia, incoming quality control is performed against the active substance master file and the manufacturer’s validated specification. The release panel includes identification, assay, related substances, residual solvents, water content, residue on ignition, elemental impurities, and microbial limits. The sterile grade carries additional bacterial endotoxin and sterility testing. The table below summarises the release attributes applied to the non-sterile milled grade; the sterile crystallized grade is released only after additional parenteral testing.
| Attribute | Method / Standard Designation | Typical Acceptance Criterion |
|---|---|---|
| Appearance | Visual inspection | White to off-white crystalline powder |
| Identification | Infrared absorption spectrophotometry, Ph. Eur. 2.2.24 | Matches reference spectrum |
| Assay on dried basis | Ion-pair reversed-phase HPLC, Ph. Eur. 2.2.29 | 98.0%–102.0% as triclobisonium chloride |
| Water content | Karl Fischer titration, Ph. Eur. 2.5.12 | ≤ 1.0% |
| Residue on ignition | Ph. Eur. 2.4.14 | ≤ 0.1% |
| Related substances | HPLC area normalisation, Ph. Eur. 2.2.29 | Single impurity ≤ 0.5%; total impurities ≤ 1.0% |
| Residual solvents | Headspace gas chromatography, Ph. Eur. 2.2.28; ICH Q3C | Class 1 solvents absent; Class 2 solvents within ICH Q3C limits |
| Elemental impurities | ICP-MS, ICH Q3D | Elemental levels within veterinary oral/parenteral PDE limits |
| Microbial limits, non-sterile grade | Ph. Eur. 2.6.12 / 2.6.13 | TAMC ≤ 10³ CFU/g; TYMC ≤ 10² CFU/g; Escherichia coli absent in 1 g |
Dry blending of the milled grade is the preferred starting point for tablets, capsules, powders, granules, and premix. Particle-size distribution is controlled by laser diffraction according to ISO 13320:2020; the non-sterile milled grade is typically supplied with D10 between 5 µm and 10 µm, D50 between 25 µm and 45 µm, and D90 ≤ 75 µm. The powder exhibits electrostatic adhesion to stainless steel and polycarbonate contact surfaces during low-humidity transfer. Surface charge dissipation with humidified nitrogen or short equilibration at 45%–55% relative humidity reduces segregation and assay loss in direct compression blends. If the API fraction is below 1.0% w/w, geometric dilution with microcrystalline cellulose or lactose monohydrate is required before addition to high-shear granulators or V-blenders.
Tablet formulations containing triclobisonium chloride should avoid anionic disintegrants such as croscarmellose sodium and sodium starch glycolate because the cationic API binds to the carboxymethyl and starch phosphate groups. Crospovidone at 2%–5% w/w is preferred as a nonionic disintegrant. Magnesium stearate at 0.5% w/w is acceptable if lubrication time is kept below 5 min; prolonged lubrication above 15 min reduces aqueous dissolution by hydrophobic coating of the API particles. Experimental batch records for a direct-compression model tablet show that a main compression force of 8 kN–15 kN and target hardness of 60 N–120 N provide disintegration times below 15 min in purified water at 37 °C according to Ph. Eur. 2.9.1. When tablet hardness exceeds 150 N, disintegration may exceed 30 min and the formulation should be rebalanced with additional nonionic disintegrant and reduced lubrication time.
Capsule filling of the API as a pure powder is limited by poor flow and hygroscopicity. Granulation with 3%–5% w/w povidone K30 and 1%–2% w/w crospovidone produces granules with bulk density between 0.45 g/mL and 0.60 g/mL, allowing reproducible dosing on a dosator-type capsule filler. Granule moisture content should be below 2.0% w/w before encapsulation to prevent capsule shell deformation and API deliquescence. Desiccant in packaging is required for climatic zones III and IV; moisture uptake above 1.0% in the API should trigger a re-drying step under vacuum at 60 °C for 4 h if stability data confirm no degradation.
For powders, granules, and premix, the API is often dispersed onto a lactose, wheat bran, or silicon dioxide carrier. The blend must be homogeneous because carryover and cross-contamination in multi-species feed mills are controlled under veterinary GMP. Dedicated equipment or validated cleaning with hot water and a nonionic detergent is required because the cationic API adheres to anionic polymer surfaces and stainless steel. Rinsates should be monitored by HPLC with a limit of quantitation of 0.1 µg/mL to verify cleaning acceptance. Swab recovery studies are performed on stainless steel coupons; recovery below 70% requires an alternative solvent system because the quaternary ammonium moiety may remain on the surface after water-only rinsing.
For parenteral use, the sterile crystallized grade is handled in an ISO 14644-1 Class 7 cleanroom within an ISO Class 5 laminar-airflow workstation. The API is dissolved in Water for Injections at 20 °C–25 °C under gentle stirring to limit foam formation. High-shear mixing is avoided because the bis-quaternary ammonium chloride can produce persistent foam that complicates sterile filtration. The solution is filtered through a 0.22 µm polyvinylidene fluoride or low protein-binding polyethersulfone membrane; nylon membranes are avoided because cationic quaternary ammonium compounds may adsorb to negatively charged nylon surfaces. Filter compatibility studies must demonstrate API recovery above 95% after the maximum batch filter load. Bacterial endotoxin testing is performed according to Ph. Eur. 2.6.14 using the kinetic chromogenic method. The acceptance criterion is calculated from the maximum recommended veterinary dose and the threshold pyrogenic dose for the target species; no universal fixed limit is applied across all injection formulations. Sterility is confirmed according to Ph. Eur. 2.6.1. Terminal sterilisation may be evaluated only after forced degradation studies confirm that the quaternary nitrogen centres are stable under the proposed thermal exposure.
Aqueous solutions are prepared with purified water at 20 °C–25 °C. The chloride salt dissolves rapidly, and pH adjustment is performed only after complete dissolution because localised alkaline conditions may trigger degradation. Oral and topical solutions are clarified through a 0.45 µm membrane, while injectable solutions require 0.22 µm filtration or terminal sterilisation after stability confirmation. The solution must not be compounded with sodium lauryl sulfate, alginates, or anionic dyes; precipitation or assay loss will occur. Packaging for aqueous solution should use Type I glass or high-density polyethylene with light protection because UV exposure in solution produces N-dealkylated degradation products detected by the related-substances HPLC method. Forced degradation studies under 0.1 M HCl, 0.1 M NaOH, and 3% H₂O₂ over 24 h are used to demonstrate method specificity and mass balance within 95%–105% before release testing.
The API is shipped in heat-sealed double low-density polyethylene liners inside a high-density polyethylene drum with a tamper-evident closure. For shipment to climatic zones III and IV, desiccant is placed between the inner and outer liner to maintain water content below 1.0% during transport. Moisture ingress is monitored by Karl Fischer titration after arrival; if water content exceeds 1.0%, the lot is quarantined and re-dried under vacuum at 60 °C for 4 h only if stability data demonstrate no degradation. The packaging is not suitable for steam sterilisation of the API; the sterile grade is produced by aseptic crystallisation or sterile filtration of the final solution. Bulk storage should avoid direct sunlight and temperatures above 30 °C unless long-term stress data are available.
Cleaning validation for equipment trains is complicated by the surface activity of triclobisonium chloride. Stainless steel and glass surfaces are rinsed with purified water at 60 °C–70 °C followed by a nonionic surfactant solution. Sodium hydroxide should not be used as the first rinse because quaternary ammonium hydroxide species may form and adhere more strongly to stainless steel. The analytical method for cleaning verification is the same stability-indicating ion-pair reversed-phase HPLC method used for assay and related substances. Limit of quantitation of 0.1 µg/mL supports detection of low residues in multi-product veterinary facilities.
Triclobisonium chloride differs from triclabendazole in chemical class and clinical application: triclabendazole is a benzimidazole anthelmintic used against liver flukes, whereas triclobisonium chloride is a bis-quaternary ammonium anti-infective used for bacterial control in veterinary dosage forms. For disinfectant or preservative applications, substitution with benzalkonium chloride is not equivalent. The bis-quaternary structure of triclobisonium has higher charge density and may shift the onset of micellar solubilisation. Direct substitution requires revalidation of minimum bactericidal concentration, surface compatibility, analytical interference, and assay recovery. Published comparative data for triclobisonium-specific critical micelle concentration and partition coefficient are limited; therefore formulation substitution is performed using experimentally generated data rather than literature extrapolation.