| HS Code | 218934 |
| Chemical Name | 4-Aminobenzenesulfonamide |
| Molecular Formula | C6H8N2O2S |
| Molecular Weight | 172.20 g/mol |
| Cas Number | 63-74-1 |
| Appearance | White or almost white crystalline powder |
| Solubility | Slightly soluble in water; sparingly soluble in ethanol; soluble in acetone, dilute mineral acids, and alkali hydroxide solutions |
| Melting Point | 164.5°C to 166.5°C |
| Assay | 99.0% to 101.0% on dried basis |
| Grade | Veterinary grade API for tablets, injections, capsules, powders, granules, premix, and solutions |
As an accredited Sulfanilamide Crystalline 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 | Sealed double-lined polyethylene bags in fiber drums, 25 kg net, with batch analysis certificate and tamper-evident closure. |
| Container Loading (20′ FCL) | 20′ FCL loading of Sulfanilamide Crystalline Veterinary Grade API, securely packed for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Sulfanilamide Crystalline (veterinary API) ships in sealed, light-resistant containers at ambient temperature, protected from moisture. Documentation includes SDS and veterinary API certificate. Not classified as dangerous goods for transport, but requires secure packaging to prevent contamination and compliance with local pharmaceutical shipping regulations. |
| Storage | Store in a tightly closed, light-resistant container in a cool, dry, well-ventilated area. Protect from moisture and direct sunlight. Avoid contact with oxidizing agents. Keep away from incompatible materials. Maintain temperatures below 25–30°C, and ensure segregation from feed and food products to prevent contamination. |
| Shelf Life | Shelf life: 24 months from manufacture date when stored in tightly sealed containers, protected from light, in a cool, dry place. |
In poultry drinking water medication, crystalline sulfanilamide API with a particle size not exceeding 250 µm is first screened through a 60-mesh stainless steel sieve to remove agglomerates. A water-soluble powder label claim of 100 mg/g active substance is obtained by a 1:9 geometric dilution of API into spray-dried lactose monohydrate. The blend contains 0.5% w/w colloidal silicon dioxide as a moisture scavenger and 1.0% w/w trisodium citrate dihydrate as a hard-water chelating aid. Mixing is performed in a V-blender charged to 60% of nominal capacity at 25 rpm for 20 minutes; blend uniformity is assessed per Ph. Eur. 2.9.40 with an acceptance RSD ≤ 5.0% across 10 sampling points. Analytical methods are validated per VICH GL18 for specificity, linearity, accuracy, and precision. The terminal product is reconstituted in drinking water through a 1:128 proportioner or a batch tank with mechanical stirring. Reconstitution is constrained by the sparing water solubility of the neutral sulfanilamide molecule, approximately 7.5 mg/mL at 25 °C. Stock solutions above 0.75% w/v require pH adjustment to 8.0–8.5 with sodium carbonate, because the weakly acidic sulfonamide nitrogen is partially deprotonated under alkaline conditions and solubility increases; however, pH above 9.0 accelerates oxidative discoloration of the primary aromatic amine. Hard water with total hardness above 250 mg/L CaCO₃ equivalence is softened or treated with citrate before dilution to reduce the precipitation risk of poorly soluble alkaline earth sulfonamide salts on drinker lines. The final solution is passed through an in-line 100 µm strainer before distribution to nipple drinkers.
Blend uniformity in top-dress oral powders is controlled less by active potency than by the cohesive nature of micronized sulfanilamide crystals and the segregation tendency of large lactose carriers. For a 250 mg/g oral powder, the API is pre-blended 1:1 with colloidal silicon dioxide and passed through a 40-mesh screen before addition to lactose monohydrate to reach a final 1:3 active-to-carrier ratio. Mixing is performed in a horizontal ribbon blender at 20 rpm for 15 minutes with a fill level of 70%; bulk density is monitored per Ph. Eur. 2.9.34 and should remain between 0.55 g/mL and 0.70 g/mL to avoid dosing cup underfill. The terminal product is administered by top-dressing over complete feed at the registered dose. Critical controls are moisture content below 2.0% by Karl Fischer titration per Ph. Eur. 2.5.12 and sieving residue below 10% retained on a 150 µm sieve. Incompatibility with copper sulfate and zinc oxide in mineral supplements requires a separate application or a chelating overcoat on the mineral granules, because sulfanilamide can form colored coordination complexes at the crystal surface under elevated moisture and temperature during summer feed-storage conditions. Sampling for blend uniformity follows ISO 6497 with a minimum of 12 increments per batch; routine release includes identity by infrared spectrophotometry per Ph. Eur. 2.2.24 and assay by HPLC with a system suitability resolution > 2.0.
Terminal steam sterilization imposes a narrow processing window for sulfanilamide injection solutions because the sulfonamide bond hydrolyses at pH extremes and elevated temperature. The crystalline API is dissolved in Water for Injections at 20 mg/mL under nitrogen sparging; the solution pH is adjusted to 8.0 with 0.1 M sodium hydroxide and maintained below 8.5. The solution is filtered through a 0.22 µm polyethersulfone membrane in a closed vessel and filled into amber Type I glass vials to limit photodegradation of the primary aromatic amine moiety. The filled vials are autoclaved at 121 °C for 15 minutes with an F₀ ≥ 12 minutes and a load probe verification at the coldest point. Published data for this specific configuration are limited; therefore, a forced-degradation study per ICH Q1A is required to quantify the hydrolysis product sulfanilic acid and related byproducts before process validation. Endotoxin control follows Ph. Eur. 2.6.14 with a limit of 0.5 EU/mg for veterinary parenteral products; sterility testing is performed per Ph. Eur. 2.6.1 using direct inoculation of 20 containers. Particulate matter is checked per USP <788> light obscuration method with limits of 6000 particles ≥ 10 µm and 600 particles ≥ 25 µm per container. The terminal product as an injectable solution must not be combined with calcium gluconate or sodium bicarbonate in the same infusion line because insoluble calcium sulfanilamide and free-base precipitation occur at pH above 9.0.
When direct compression is selected for companion animal tablets, the crystalline API is delumped through a 0.5 mm screen and attrited to a particle size distribution with d50 75 µm and d90 150 µm. A label claim of 50 mg per tablet is achieved with a 1:4 active-to-filler ratio using microcrystalline cellulose and anhydrous lactose in equal parts; crospovidone at 2.0% w/w is added as a disintegrant, and magnesium stearate at 0.5% w/w is screened through a 60-mesh sieve before final lubrication. The blend is compressed on a rotary tablet press fitted with 8 mm round B-tooling at a compression force of 8–12 kN; tablet hardness is held between 7 kp and 10 kp because lower hardness causes edge chipping during film coating or packaging, while higher hardness retards disintegration. The terminal tablet is tested for friability per USP <1216> with a weight loss ≤ 1.0% after 100 revolutions, disintegration per USP <701> in purified water at 37 °C with a limit of 15 minutes, and dissolution per USP <711> Apparatus 2 in 900 mL of 0.1 M hydrochloric acid at 50 rpm; the dissolution criterion is Q = 75% at 45 minutes. Content uniformity per Ph. Eur. 2.9.40 is applied to 10 dosage units with an acceptance value ≤ 15. Film coating with HPMC-based systems is conducted at a product bed temperature of 38–42 °C to avoid moisture uptake above 2.0% and subsequent hydrolytic degradation during shelf life.
Powder flow into size 3 hard gelatin capsules is controlled by the angle of repose and compressibility of the diluted API blend. A label claim of 50 mg per capsule requires a 1:5 API-to-filler ratio with pregelatinized starch and lactose monohydrate; the blend is lubricated with 0.25% w/w magnesium stearate after a preliminary 10-minute mixing cycle. Powder flow is assessed per USP <1174> with an angle of repose ≤ 40° and a compressibility index ≤ 25%; if flow fails, colloidal silicon dioxide is added in 0.25% increments up to 1.0% w/w. Capsule filling is conducted on a tamping-pin machine with five tamping pins set to 12 mm penetration depth and a target fill weight of 300 mg ± 5%. Weight variation follows Ph. Eur. 2.9.5 for hard capsules; dissolution for the capsule product uses USP <711> Apparatus 1 at 100 rpm in 900 mL of 0.1 M hydrochloric acid with Q = 75% at 45 minutes. Because the gelatin shell is hygroscopic, bulk packaging is executed below 25 °C and 40% relative humidity to prevent shell crosslinking, which would delay dissolution.
Dry blending into mineral premixes introduces contact alkalinity and trace metal redox interfaces that can degrade sulfanilamide during storage. A 10% w/w sulfanilamide premix is manufactured by wet granulation to reduce segregation and dust. The crystalline API is first dry-mixed 1:1 with microcrystalline cellulose in a high-shear granulator at impeller speed 300 rpm for 5 minutes; purified water is added at 12% w/w as the granulation liquid, and wet massing continues at 150 rpm for 8 minutes. The wet granules are then dried in a fluid bed dryer with inlet air at 60 °C and product temperature maintained below 40 °C until loss on drying is 2.0–3.0% by Ph. Eur. 2.2.32. Dried granules are sized through a 1.0 mm screen; the target granule fraction 0.8–1.4 mm should represent at least 80% of the batch to avoid segregation when mixed into a feed mill batch. The finished premix is diluted into complete feed at a rate specified by the marketing authorization; blend homogeneity after 10 minutes in a horizontal mixer is verified per ISO 6497. The terminal product as a medicated feed premix must not contain free calcium oxide above 2.0% w/w or copper and zinc above 250 mg/kg in the same dry formulation, because these agents produce alkaline microenvironments and redox-active metal ions that accelerate oxidative degradation of the primary aromatic amine. If such combinations are unavoidable, a physical barrier coating on the mineral particles and a desiccant-lined package are used; shelf-life is established by a real-time stability study in the proposed package under ICH Q1A conditions for the intended climatic zone.
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Sulfanilamide Crystalline Veterinary Grade API is the unsubstituted para-aminobenzenesulfonamide, CAS 63-74-1, with molecular formula C6H8N2O2S and molecular weight 172.20 g/mol. The crystalline material is a white to off-white powder intended for incorporation into tablets, injections, capsules, powders, granules, premix, and solutions for veterinary antimicrobial therapy. Manufacturer model designations separate unmicronized crystalline grade, micronized grade with D90 ≤50 µm, and injectable low-endotoxin grade; these material-class suffixes are logistical identifiers and do not replace compendial identity. Sulfanilamide contains a primary aromatic amine and a sulfonamide group, which together control diazotization titration, oxidative degradation behavior, and excipient compatibility.
The veterinary grade is controlled against compendial methods where applicable. Release specifications generally include assay on the anhydrous basis at 98.0–102.0%, loss on drying ≤0.5% after 105 °C for 2 h, residue on ignition ≤0.1%, and melting range 164–166 °C. Related substances are determined by stability-indicating HPLC. Residual solvent and microbial quality are additionally controlled according to USP <467> and USP <61>/USP <62>. Particle-size distribution and bulk density are reported in the manufacturer certificate of analysis because they alter downstream processing in every dosage form listed.
Table 1 lists representative release parameters for a crystalline veterinary grade. Specific acceptance criteria may vary by compendial edition, manufacturing site, and grade designation.
| Parameter | Acceptance criterion | Test method |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual / microscopic |
| Identification | IR spectrum consistent with sulfanilamide CRS | IR absorption spectrophotometry |
| Assay (anhydrous basis) | 98.0–102.0% | HPLC or diazotization titration |
| Melting range | 164–166 °C | USP <741> |
| Loss on drying | ≤0.5% after 105 °C for 2 h | USP <731> |
| Residue on ignition | ≤0.1% | USP <281> |
| Related substances | Total impurities ≤1.0% | Stability-indicating HPLC |
| Residual solvents | Meet Class 2 and Class 3 limits | USP <467> |
| Particle size, micronized grade | D90 ≤50 µm; D50 10–30 µm | Laser diffraction ISO 13320:2020 |
| Bulk density | Site-specific range reported on CoA | USP <616> |
| Microbial enumeration, nonsterile grade | TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g | USP <61>/USP <62> |
| Bacterial endotoxins, injectable grade | Dose-specific low-endotoxin limit; not a routine numeric release value without finished product risk assessment | USP <85> |
Crystal habit and particle-size distribution produce opposing effects on formulation performance. Micronized sulfanilamide increases specific surface area and reduces dissolution lag in immediate-release tablets and oral suspensions, but it also increases cohesivity and static charge. Laser diffraction particle sizing according to ISO 13320:2020 is used to monitor D10, D50, and D90; a micronized veterinary grade typically has D90 ≤50 µm and D50 10–30 µm. When the D90 falls below 20 µm, the Carr compressibility index may exceed 25% and the Hausner ratio may exceed 1.34, which is a recognized powder-flow boundary for tablet compression. At this limit, direct compression is generally not robust, and dry granulation or wet granulation is required. Powder flow testing under USP <1174> is used to establish the blend and lubrication end point.
Jet milling and hammer milling introduce surface amorphization and modify bulk density. X-ray powder diffraction is used to confirm that the crystalline phase remains within the approved pattern, because surface amorphous content above site-specific thresholds can increase moisture sorption and chemical degradation. Drying of wet-cake material at temperatures above 70 °C can produce yellowing or melting point depression if residual solvent or impurities are present; therefore, controlled vacuum drying or forced-air drying with product temperature monitoring is standard. The unmicronized crystalline grade is preferred when granulation strength and densification are required, while the micronized grade is selected for low-dose content uniformity and rapid dissolution. Published data for the polymorphic transformation boundaries of this specific veterinary grade is limited; site-specific XRPD and moisture sorption profiles are required.
Tablet processing of sulfanilamide veterinary grade begins with particle-size selection and excipient compatibility screening. The API can be blended with microcrystalline cellulose, dicalcium phosphate, and sodium starch glycolate. Lactose-based diluents should be avoided in wet granulation because the primary aromatic amine can participate in Maillard-type degradation under heat and moisture. For low-dose tablets, a micronized grade with D90 ≤20 µm is preferred for blend uniformity, but flow function coefficients may be low; roller compaction with screen milling is then used to restore granule density. Blend uniformity is evaluated by unit-dose sampling and HPLC assay, with acceptance typically set at RSD ≤5.0%. Finished tablets should meet USP <905> uniformity of dosage units, USP <701> disintegration, and USP <711> dissolution where a monograph exists.
Over-blending with magnesium stearate beyond 5 min can delay dissolution through hydrophobic surface coverage; lubrication time and mixer speed are therefore controlled. Tablet hardness, friability per USP <1216>, and moisture content are monitored after compression. Capsule filling of sulfanilamide-containing blends requires control of powder flow and segregation; force-feeding equipment on rotary capsule fillers may densify the blend and alter dissolution. In-line bulk density and weight variation are monitored during filling. For capsules, dissolution testing is conducted with sink conditions that account for the sparing aqueous solubility of the unsubstituted sulfonamide, and media volumes may require pH 6.8 phosphate buffer or dilute hydrochloric acid to demonstrate complete release.
Production-scale failure modes in high-shear and low-shear blending include segregation of micronized API to the top of V-blenders and static adhesion to polyvinyl chloride transfer tubing. These failure modes are managed by grounding, humidity control, and order-of-addition sequencing. For roller compaction, insufficient roll pressure can generate weak ribbons that increase fines and compressibility index, while excessive pressure can reduce tablet dissolution by increasing granule hardness. Granule density is measured by tapped density and sieve retention, and compression settings are adjusted based on tablet hardness and disintegration time.
Injectable formulations require low-endotoxin sulfanilamide and strict control of solution clarity. Because sulfanilamide is sparingly soluble in water, liquid formulations frequently use co-solvents such as propylene glycol, glycerin, or dilute ethanol; pH adjustment may be used to form the more soluble sodium salt, but physiological pH and tissue compatibility limit the degree of alkalinization. Terminal steam sterilization at 121 °C for 15 min cannot be assumed to be stability-neutral for all formulations; aseptic filtration through a 0.22 µm membrane is often evaluated, and the final filled solution should comply with USP <71> sterility, USP <85> bacterial endotoxins, and USP <788> particulate matter.
Stability of injectable sulfanilamide solutions may be affected by light, oxygen, and trace transition metals. Nitrogen blanketing and chelating agents such as disodium edetate are evaluated when discoloration is observed during forced-degradation studies. Because sulfanilamide has a primary aromatic amine, oxidative coupling can generate colored by-products; filters, tubing, and container closures should be selected for low metal ion release. Published data for this specific injectable configuration is limited, so route-specific stability protocols are required before batch release.
Stability-indicating HPLC methods for sulfanilamide veterinary grade typically separate sulfanilamide from sulfanilic acid and related sulfonamide impurities. Diazotization titration is suitable for assay of the unsubstituted primary aromatic amine content, but it is not stability-indicating when degradants retain the primary amine. Forced-degradation studies include acid, base, oxidative, thermal, and photolytic conditions; mass balance is required in the range of 95–105% unless degradation products are identified. The crystalline API should show no significant change at 40 °C / 75% RH over 6 months in accelerated stability protocols, but site-specific data are required for each grade and container-closure system.
Powders, granules, and premix formulations for veterinary feed use are produced by stepwise dilution of the API onto carriers such as ground corn, rice hulls, or lactose. Mixing is performed in ribbon or paddle mixers; mixer speed, fill level, and mixing time are validated by thief sampling and HPLC assay. Homogeneity acceptance for medicated premix is often set at pooled RSD ≤5.0% for active concentration; lower RSD limits may apply when the final feed inclusion rate is low. Segregation in bulk bins and screw conveyors is controlled by matching API particle size to carrier particle size and by avoiding excessive fines generation. Granules may be prepared by wet massing, extrusion-spheronization, or fluid-bed granulation using binders that do not contain primary amine-reactive aldehydes.
Oral solutions and soluble powders for drinking-water administration require a soluble salt, pH adjustment, or co-solvent. Sulfanilamide base is sparingly soluble in water, so oral solutions frequently use sodium sulfanilamide or buffered vehicles; soluble powder formulations may contain buffering agents to maintain dissolution in hard water. Hard water ions and acidic metal salts can reduce clarity; water quality testing for hardness and iron content is recommended before field use. Protection from light in final containers reduces photochemical discoloration. In all nonsterile powder and solution lines, cleaning validation must prevent cross-contamination into non-sulfonamide feed lines because sulfonamide residues in food-producing animals are regulated in edible tissues and milk.
Sulfanilamide differs from later sulfonamide APIs chiefly in molecular weight, potency, solubility, and metabolism. It lacks the pyrimidinyl, methoxy, or methyl substituents that increase antibacterial potency and extend elimination half-life. Consequently, veterinary formulations containing sulfanilamide often use higher dose rates and shorter dosing intervals than formulations containing sulfadiazine or sulfadimethoxine. The unsubstituted structure also produces a polar molecule with lower lipid solubility; this can reduce tissue penetration but favors renal excretion. The mechanism of action remains competitive inhibition of dihydropteroate synthase, so cross-resistance with other sulfonamides is expected. Minimum inhibitory concentrations are isolate-specific, and susceptibility testing is required for clinical efficacy claims.
Differentiating physical and chemical properties are shown in Table 2. Potentiated combinations require simultaneous assay of two actives and ratio uniformity, while single sulfanilamide products require sulfonamide-related impurity tracking. The primary aromatic amine in sulfanilamide is analytically active in diazotization titration; it also imposes constraints against aldehyde-containing excipients, nitrite salts, and strong oxidizing agents. Sulfanilamide should not be combined with local anesthetics containing para-aminobenzoic acid derivatives, because para-aminobenzoic acid antagonism can reduce antibacterial activity.
| Feature | Sulfanilamide Veterinary Grade | Sulfadiazine | Potentiated Sulfonamide Combination |
|---|---|---|---|
| Molecular weight | 172.20 g/mol | 250.28 g/mol | Combination-specific |
| Substituent chemistry | None; unsubstituted para-aminobenzenesulfonamide | Pyrimidine-substituted sulfonamide | Sulfonamide plus diaminopyrimidine |
| Water solubility | Sparingly soluble in water; soluble in ethanol, acetone, dilute acid | Practically insoluble in water; sodium salt used for injection | Combination-specific; often suspension or co-solvent |
| Formulation implications | Higher dose rates and shorter dosing intervals; more pH-dependent solubility | Lower dose rates; parenteral sodium salt | Fixed-ratio stability and dissolution matching; assay for both actives |
| Analytical marker | Primary aromatic amine by diazotization; HPLC for related sulfonamides | HPLC with pyrimidine-related impurities | Simultaneous assay and ratio uniformity |
| Compatibility boundaries | Avoid aldehyde-functional excipients, nitrite salts, and oxidizing agents | Avoid PABA-derived excipients; sodium salt precipitation risk | Ratio disturbances from excipient interaction |
Selection of sulfanilamide instead of a substituted sulfonamide should be based on approved target species, residue depletion data, and local regulatory status. Sulfanilamide has an extensive historical toxicology database, but acquired resistance is documented across veterinary isolates. Regulatory acceptance and withdrawal periods for food-producing species are jurisdiction-specific; in some markets, use in lactating dairy cattle is restricted or prohibited due to milk residue concerns.
The crystalline veterinary grade is stored in well-closed containers under light protection at controlled room temperature, typically 20–25 °C with excursions defined by the manufacturer. High relative humidity above 60% can increase particle agglomeration and reduce flow; pre-drying may be required before dry processing. Sulfanilamide is incompatible with strong oxidizing agents, nitrite salts, and aldehyde-functional excipients under moist conditions. Contact with copper or iron can promote discoloration in solution; stainless steel or glass-lined equipment is used for liquid manufacturing. Containers should be resealed promptly after use to limit exposure to oxygen and moisture.
For injectable and oral solution manufacturing, aqueous stock solutions are prepared fresh or held under controlled temperature and light conditions after chemical and microbiological stability data are generated. Prolonged storage of alkaline sulfanilamide solutions can increase hydrolysis or oxidative degradation, so pH and color are monitored as in-process controls. Microbial limits for nonsterile dosage forms should comply with USP <61> and USP <62>; objectionable organisms such as Escherichia coli and Salmonella are absent by site-specific test methods. Industrial hygiene controls include dust extraction and local exhaust ventilation when handling micronized powder, because sulfonamide hypersensitivity reactions are documented in exposed workers.