| HS Code | 454399 |
| Product Name | Neoasphenamine Veterinary Grade API |
| Synonyms | Neoarsphenamine; Neosalvarsan; Novarsenobenzol; Neoarsenobenzol |
| Cas Number | 457-60-3 |
| Molecular Formula | C13H13As2N2NaO4S |
| Molecular Weight | 546.15 g/mol |
| Appearance | Yellow to yellow-brown powder |
| Odor | Odorless or faint characteristic odor |
| Solubility | Soluble in water; slightly soluble in ethanol; practically insoluble in ether and chloroform |
| Ph | 6.5 to 8.5 (aqueous solution) |
| Stability | Light-sensitive and hygroscopic; decomposes on exposure to air and light |
| Storage Conditions | Store in a cool, dry, dark place; keep container tightly closed |
| Shelf Life | 24 to 36 months when stored properly |
| Purity | ≥98% (veterinary grade) |
| Grade | Veterinary Grade API |
| Dosage Forms | Tablets, injections, capsules, powders, granules, premix, solutions |
| Packaging | Foil bags, fiber drums, or as per customer requirements |
| Usage | For veterinary pharmaceutical manufacturing and compounding |
| Therapeutic Category | Antiprotozoal; arsenical |
| Target Species | Cattle, sheep, horses, camels, dogs |
| Toxicity | Toxic; arsenical compound; handle with care |
As an accredited Neoasphenamine 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 | Neoasphenamine Veterinary Grade API packaged in 25 kg double-lined fiber drums, sealed; suitable for tablets, injections, capsules, powders, granules, premix, solutions. |
| Container Loading (20′ FCL) | Neoasphenamine Veterinary Grade API loaded in a 20′ FCL container, suitable for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Neoasphenamine Veterinary Grade API is shipped in sealed, light-resistant, moisture-proof containers under controlled temperature, with batch-specific COA/SDS documentation. Packaging complies with IATA/ADR/IMDG regulations where applicable, preventing contamination, leakage, or degradation during transport for tablets, injections, capsules, powders, granules, premixes, and solutions. |
| Storage | Store Neoasphenamine Veterinary Grade API in tightly sealed, light-resistant containers under controlled room temperature (15–25°C), in a cool, dry, well-ventilated, secure area. Protect from moisture, air, heat, direct sunlight, and freezing (solutions). Segregate from food, feed, acids, and oxidizers. Use secondary containment and follow SDS, pharmacopeial, and local regulations. For veterinary use only. Keep containers closed when not in use. |
| Shelf Life | Neoasphenamine Veterinary Grade API shelf life depends on dosage form and storage; keep sealed, cool, dry, protected from light/oxygen. Follow manufacturer’s expiration date. |
For tablet-grade neoasphenamine in jurisdictions where the substance remains authorized for veterinary medicinal products, direct compression is preferred over wet granulation because aqueous granulation fluids accelerate oxidative discoloration and generate agglomerates with poor rework behaviour. A production-scale batch is typically dried to a loss on drying value below 1.0% w/w before blending. The API fraction is passed through a screen with a mesh aperture of 250 µm to break deliquescent aggregates; any retained material above 5.0% w/w after 20 minutes of screening indicates an over-dried or electrostatically charged lot. The standard tablet formula is assembled as follows: neoasphenamine 50.0 mg per unit, microcrystalline cellulose q.s. to 200.0 mg core weight, crospovidone 2.0% w/w as disintegrant, and magnesium stearate 0.5% w/w as lubricant. Magnesium stearate is limited to 0.5% w/w because higher concentrations extend disintegration beyond 15 minutes when measured by Ph. Eur. 2.9.1. Compression is performed on a rotary tablet press fitted with multi-tip tooling at 8–15 kN compression force and 30–60 rpm turret speed. The hardness target is 40–80 N by Ph. Eur. 2.9.8, and friability is required to remain below 1.0% w/w by Ph. Eur. 2.9.7. Blend uniformity is tested by stratified sampling at 10 positions with an acceptance of ≤5.0% RSD per Ph. Eur. 2.9.40. Finished tablets are packaged in aluminium/aluminium blister cavities with a desiccant sachet because the API oxidizes under sustained relative humidity above 60% RH.
Aqueous stability of neoasphenamine is the principal constraint that dictates aseptic powder filling or lyophilization rather than terminal sterilization. The fixed-dose form is prepared as a powder for injection because aqueous solutions darken rapidly when dissolved oxygen is present. In a lyophilized configuration, the API is dissolved in Water for Injections at 5–10 °C; the solution is adjusted to pH 8.0–9.0 with 0.1 M sodium carbonate or dilute sodium hydroxide where the approved veterinary monograph permits alkaline adjustment. The solution is sterile-filtered through a 0.22 µm membrane into Type I borosilicate glass vials. Headspace oxygen is reduced to ≤1.0% v/v by nitrogen overlay before sealing. Lyophilization proceeds by freezing to -40 °C at a controlled ramp, primary drying at -20 °C for 24–36 hours, and secondary drying at 20–25 °C until residual moisture is ≤2.0% w/w by USP <921> Method Ia. Sterility is confirmed per Ph. Eur. 2.6.1 or USP <71>. Particulate matter is controlled per USP <788> for small-volume injection: not more than 6000 particles per container at ≥10 µm and not more than 600 particles per container at ≥25 µm. Aseptic production follows EU GMP Annex 1 and requires closed containment because the substance is an arsenical powder with a typical occupational exposure band of 4. Terminal steam sterilization is not used because thermal degradation generates unidentified oxidation products and shifts the pH beyond the permitted limit.
Hard gelatin capsule filling with neoasphenamine requires environmental control below 30% RH and product temperature below 25 °C to prevent shell softening and API particle aggregation. The blend for a size 3 capsule typically consists of neoasphenamine 100.0 mg, lactose monohydrate q.s. to 250.0 mg, pregelatinized starch 5.0% w/w, and sodium stearyl fumarate 1.0% w/w. Magnesium stearate is excluded from the capsule formulation because its hydrophobic film can delay dissolution when the fill is compressed; sodium stearyl fumarate provides lubrication without the same moisture migration effect. Fill weight variation is monitored per USP <905> or Ph. Eur. 2.9.40 with an acceptance of ≤5.0% RSD for content uniformity. The filling machine is operated with dosator or tamping-pin tooling at 40–70% of rated line speed; higher speed increases dusting and charge separation of the API. Capsules are sealed after filling to reduce oxygen exchange through the shell. Dissolution testing is performed in 900 mL water at 37.0 ± 0.5 °C with paddle speed 50 rpm according to Ph. Eur. 2.9.3; release is considered valid when the measured dissolved fraction meets the authorized veterinary product specification. Moisture-sensitive batches are packed in HDPE bottles with silica gel canisters if the capsule shell retains more than 13–16% w/w shell moisture at the point of filling.
Following dry blending of neoasphenamine with a buffered carrier, the powder is filled into sachets for reconstitution as an oral solution. The carrier contains anhydrous dibasic sodium phosphate and a citrate buffer to bring the reconstituted solution to pH 8.0–9.0. Blend uniformity is tested across 10 sampling points with an acceptance of ≤5.0% RSD per Ph. Eur. 2.9.40. Single-dose fill weight variation is controlled per Ph. Eur. 2.9.5, with a maximum deviation of ±7.5% from the labelled fill weight. Bulk density and tapped density are measured by USP <616>; Carr's index is maintained at ≤25% to prevent bridging in the sachet filling head. The powder is filled into laminated aluminium foil sachets with a water vapour transmission rate below 0.1 g/m²/day. The reconstituted solution is prepared with potable water at 20–25 °C and is used within 2 hours unless visible darkening or precipitate occurs earlier. Published data for this specific configuration is limited; therefore, accelerated stability screening at 40 °C/75% RH is required to confirm that the buffered carrier does not accelerate discoloration of the arsenical API. The terminal product is labelled for single-dose use because in-use storage of the reconstituted solution exceeds the known oxidative stability boundary.
| Dosage form | Critical parameter | Test method or standard | Acceptance window | Operational boundary |
| Tablet core | Blend uniformity | Ph. Eur. 2.9.40 | ≤5.0% RSD | Direct compression only if LOD <1.0% w/w |
| Tablet core | Resistance to crushing | Ph. Eur. 2.9.8 | 40–80 N | Above 80 N disintegration may exceed 15 min |
| Tablet core | Friability | Ph. Eur. 2.9.7 | ≤1.0% w/w | Reject if capping occurs above 15 kN |
| Injection lyophilized | Residual moisture | USP <921> Method Ia | ≤2.0% w/w | Higher moisture reduces in-use stability |
| Injection | Particulate matter | USP <788> | SVP limits | Aseptic processing; no terminal sterilization |
| Capsule | Content uniformity | USP <905> / Ph. Eur. 2.9.40 | ≤5.0% RSD | RH above 30% is outside boundary |
| Oral powder | Bulk and tapped density | USP <616> | Carr's index ≤25% | Above 25% adjust glidant level |
| Premix | Mix uniformity | In-house tracer, 10-point sampling | ≤5.0% CV | Extend mix time only after dead-spot check |
| Drench solution | Water content | USP <921> Method Ia | ≤2.0% v/v | Non-aqueous vehicle only; higher water accelerates degradation |
Granules intended for veterinary in-feed application are manufactured as low-potency premixes to ensure homogeneous dilution into final feed. A standard batch uses neoasphenamine pre-blended at 10.0% w/w active concentration onto a lactose or calcium carbonate carrier. The carrier particle size is controlled to a D90 of 150–300 µm to reduce segregation during pneumatic or screw conveying. Mixing is carried out in a ribbon blender filled to 60–70% of rated capacity at 20 rpm for 10–15 minutes; blend time is validated by a tracer test with a coefficient of variation ≤5.0% across 10 sampling points. The premix is packed in multi-wall paper sacks with a polyethylene liner, and storage relative humidity is held at ≤50% RH. In the final feed compounder, the premix is diluted to the authorized veterinary feed inclusion rate; carryover is controlled by sequencing flush batches after the arsenical premix run. Residual arsenic in the next non-medicated batch is tested by atomic absorption spectrophotometry where zero-tolerance residue policy is enforced. Medicated feed facilities in U.S.-style regulatory systems follow 21 CFR 225 current good manufacturing practice for medicated feeds, but regional authorization of arsenical feed additives is not uniform. The terminal product is a stable granule premix only if the carrier is dry and free of reducing sugars; incompatibility with reducing sugars can lead to darkened granule surfaces and loss of active content.
Oral drench solutions containing neoasphenamine require a non-aqueous vehicle when aqueous reconstitution is not feasible for field administration. Published data for this specific configuration is limited; formulation screening is therefore required to determine saturation solubility and oxidative stability before batch manufacture. The candidate vehicle is selected from propylene glycol, glycerol formal, or polyethylene glycol 400. Initial loading is adjusted only after solubility screening above 50 mg/mL at 25 °C is demonstrated for the chosen vehicle. Water content is controlled below 2.0% v/v by USP <921> Method Ia. The solution is manufactured in a closed stainless-steel vessel under nitrogen blanketing, filtered through a 10 µm duplex filter, and filled into amber Type III glass or HDPE bottles with fluoropolymer seals. Viscosity is measured using a rotational viscometer at 25 °C; the target range is 50–500 mPa·s to maintain dose accuracy from standard drench guns. The terminal product is protected from light because the liquid form is more sensitive to ultraviolet exposure than the dry powder form. Polycarbonate contact surfaces are avoided during manufacturing because solvent interaction with the vehicle can release extractables. The drench solution is assigned a short in-use shelf life after first opening unless a multi-dose stability study demonstrates otherwise.
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Neoasphenamine Veterinary Grade API is a vacuum-dried complex organoarsenical supplied under release model NEOASP-VET-API-2407 for downstream formulation into tablets, injections, capsules, powders, granules, premixes, and solutions. The bulk powder appears as a pale yellow to light brown amorphous solid. It is manufactured as a veterinary pharmaceutical intermediate and is not a finished dose form. Compendial alignment relies on general pharmacopoeial methods for organoarsenical purity, elemental impurities, residual solvents, and microbial quality because a product-specific harmonized monograph is not currently published. Published data for this specific configuration is limited; release limits should therefore be justified from registration batches and stability studies rather than assumed from human arsenical monographs.
The main differentiation in this grade is the reduction of free aromatic amine content and the control of inorganic arsenic below the threshold applicable to parenteral and oral veterinary formulations. Typical batch documentation includes assay by high-performance liquid chromatography against a qualified reference standard, total arsenic by inductively coupled plasma mass spectrometry, speciation for trivalent and pentavalent inorganic arsenic, water content, particle-size distribution, and bacterial endotoxin for parenteral grades. The material is intended for use under marketing authorization or compounding authorization in the destination jurisdiction.
Assay is performed by reversed-phase high-performance liquid chromatography with ultraviolet detection using a C18 column of 150 mm length and 4.6 mm internal diameter, with a mobile-phase buffer at pH 8.0 and an acetonitrile gradient. Quantification against a qualified reference standard is used, and peak homogeneity is assessed by photodiode array. Mass balance is confirmed by total arsenic determination using inductively coupled plasma mass spectrometry according to USP <233>; speciation for inorganic arsenite and arsenate is included in the impurity profile. Residual solvent control is applied according to USP <467> or Ph. Eur. 2.4.24.
Oxidative discoloration and precipitation in aqueous vehicle systems are controlled primarily by headspace oxygen exclusion, low-temperature handling, and pH buffering. In production-scale compounding, the API is dissolved in water for injection that has been sparged with pharmaceutical-grade nitrogen until dissolved oxygen is below 2 mg/L. Vessels are blanketed with nitrogen to maintain residual headspace oxygen below 5% v/v. Solution temperature is held at 5–15°C during mixing and filling because the degradation rate increases rapidly above ambient temperature; published data for this specific configuration is limited, but pilot-batch observations show visible darkening when the temperature exceeds 25°C for periods longer than 90 min. The pH is maintained in the range 7.4–8.0 using a phosphate or borate buffer; below pH 6.5 acid-catalyzed cleavage of the arsenobenzene linkage becomes more evident.
Transition-metal ions, particularly iron(III) and copper(II), accelerate oxidation at trace concentrations. Compounding equipment constructed of 316L stainless steel or glass is preferred. Rubber closures used for injection vials require halogenated stoppers with a low extractable profile; butyl closures without fluoropolymer coating may release metal ions and should be evaluated under Ph. Eur. 3.2.9. The preparation of solutions should be performed under sodium vapour or amber light protection because ultraviolet exposure increases free-radical oxidation. Avoid combination with sulfhydryl-containing excipients, ascorbic acid, and sodium metabisulfite because these reducing agents promote precipitation of arsenic intermediates.
The specification matrix for Neoasphenamine Veterinary Grade API is route-dependent. Solid oral premix and granulation grades tolerate wider residual water and particle-size limits than parenteral grades. Parenteral-grade material is tested for bacterial endotoxin and subvisible particulate matter when the finished product is a solution for injection. The table below summarizes general release criteria applied to the bulk API; final registration limits must be confirmed by the finished-product marketing authorization holder.
| Parameter | Method or Reference Standard | Release Criterion |
|---|---|---|
| Appearance | Visual inspection against reference standard | Pale yellow to light brown amorphous powder |
| Water content | USP <921> / Ph. Eur. 2.5.12 | ≤2.0% w/w for solid grades; ≤5.0% w/w where declared as hydrated complex |
| Particle size, D90 | USP <786> / Ph. Eur. 2.9.31 | ≤75 µm for parenteral suspension; ≤250 µm for premix and direct compression |
| Bulk density | USP <616> Method I | 0.35–0.55 g/mL |
| Bacterial endotoxins | Ph. Eur. 2.6.14 / USP <85> | <2.5 EU/mg for parenteral grade; oral grade controlled by risk assessment |
| Total aerobic microbial count | USP <61> / Ph. Eur. 2.6.12 | ≤10² CFU/g |
| Elemental impurities | USP <232>/<233>, ICH Q3D | Class 1 and 2A limits applied; arsenic controlled separately by mass balance |
Residual solvent control is applied according to USP <467> or Ph. Eur. 2.4.24. Methanol, acetone, and isopropyl alcohol are the principal solvents screened in the process validation protocol. No Class 1 solvent should be present above the concentration limit of 5 ppm for benzene and 5 ppm for carbon tetrachloride when calculated by the standard option. Storage in sealed amber glass containers under nitrogen at 2–8°C is required for re-test periods exceeding 12 months.
Process experience from pilot and production-scale blending lines indicates that the powder exhibits cohesive flow behaviour at bulk densities below 0.40 g/mL; die fill variation increases when the material is subjected to storage at relative humidity above 60% without desiccant. Pre-drying at 25–30°C under vacuum for 4–6 h restores flow for direct encapsulation. Equipment surfaces should be earthed because the dry powder can accumulate static charge during transfer through flexible hoses. Dispensing in a low-humidity glovebox or laminar flow booth is recommended, with ambient exposure limited to less than 30 min per dispensing event.
For premix and granulation applications, the API is first diluted with a carrier such as lactose monohydrate, calcium carbonate, or ground rice hulls. Low-shear tumble blending at 10–25 rpm for 10–20 min is preferred; high-shear granulation exposes the API to localized temperature rise above 40°C, which can accelerate oxidative degradation. Addition of 0.05–0.20% w/w colloidal silicon dioxide reduces segregation and improves flow without a significant effect on dissolution. The inclusion of reducing sugars should be avoided because they promote reduction and precipitation of arsenic intermediates. If molasses or dextrose carriers are required by the feed formulation, a compatibility study under 25°C/60% RH for 14 days should be conducted before scale-up.
Granule particle-size distribution is controlled by sieve analysis with a target of 90% by weight between 180 µm and 1000 µm for free-flowing premix. Overmixing beyond 20 min can generate fines that segregate during pneumatic conveying. Batch-to-batch variation in bulk density was observed on a 500 kg ribbon-type mixer when carrier moisture varied by more than 1.5% w/w. Equipment contact surfaces should be non-reactive; carbon steel is not recommended because surface iron can accelerate oxidative discoloration and increase the inorganic arsenic fraction during extended storage.
For tablet and capsule manufacture, direct compression or dry granulation is preferred over wet granulation because aqueous granulation solvents increase hydrolysis and require subsequent drying that can accelerate oxidation. Roller compaction at specific force of 8–12 kN/cm with 0.5–1.0 mm screen milling has produced granules suitable for capsule filling. Magnesium stearate at 0.5% w/w is typically compatible, but talc from unvalidated sources should be avoided because trace metal contamination can affect stability. Tablet hardness should be managed to avoid excessive compaction; target friability below 1.0% under USP <1216> is generally sufficient for downstream coating.
Neoasphenamine differs from arsphenamine dihydrochloride in aqueous solubility, pH after dissolution, and parenteral formulation suitability. Arsphenamine requires dissolution in alkaline solution before injection and is not supplied as a ready-to-compound neutral salt. Neoasphenamine carries a N-methylene sulfinate/sulfonate substitution that increases water solubility and lowers free aromatic amine reactivity; however, oxidation sensitivity remains a critical control point. Roxarsone and related phenylarsonic acid feed additives are used in different livestock production contexts and have different regulatory status; they are not interchangeable with Neoasphenamine in injectable or tablet formulations.
| Property | Neoasphenamine Veterinary Grade API | Arsphenamine dihydrochloride | Roxarsone-type feed additive |
|---|---|---|---|
| Aqueous solubility at 20°C | Freely soluble, alkaline solution | Sparingly soluble; requires alkaline solubilization | Variable; often supplied as sodium salt |
| Free aromatic amine | Reduced by substitution | High | Not applicable to nitro/arsonic acid structure |
| Primary formulation routes | Injection, tablet, capsule, premix, solution | Parenteral historical use only | Feed premix |
| Oxidation sensitivity | High; requires nitrogen blanketing | Very high; air-sensitive | Lower under dry conditions |
| Regulatory alignment | Veterinary API; route-specific controls | Historical monograph only | Feed additive; food animal restrictions apply |
For solution dosage forms intended for parenteral administration, Neoasphenamine is dissolved in water for injection under nitrogen and filtered through a 0.22 µm membrane. Terminal sterilisation is not generally applied because of thermal sensitivity; aseptic processing is used. Tonicity adjustment is performed with sodium chloride at 9.0 g/L, and the pH is adjusted with dilute sodium hydroxide or hydrochloric acid. The finished solution should be filled into amber Type I glass vials under nitrogen and stored at 2–8°C. Long-term storage beyond 24 h at room temperature is not recommended because of colour change and precipitation. For oral solutions, similar principles apply, but short-term stability may be improved by using a non-reducing vehicle system and avoiding metal-ion contamination.
The API should not be exposed to open air for extended periods after the primary container is opened. Once opened, the container should be re-sealed under nitrogen and returned to refrigerated storage. Any material that has become dark brown, sticky, or shows visible particulate formation after reconstitution should be rejected. These operational boundaries are essential because the organoarsenical backbone is prone to oxygen- and light-mediated transformation, and the resulting impurity profile can shift outside the validated specification range for parenteral or oral veterinary use.