| HS Code | 740369 |
| Product Name | Sulphamethoxypyridazine Base Pharma Grade API |
| Chemical Name | 4-Amino-N-(6-methoxy-3-pyridazinyl)benzenesulfonamide |
| Cas Registry Number | 80-35-3 |
| Molecular Formula | C11H12N4O3S |
| Molecular Weight | 280.30 g/mol |
| Physical Form | White to off-white crystalline powder |
| Solubility | Very slightly soluble in water; sparingly soluble in ethanol; soluble in dilute mineral acids and dilute alkali hydroxide solutions |
| Melting Point | 180 to 183 °C |
| Therapeutic Category | Long-acting sulfonamide antibacterial |
| Mechanism Of Action | Inhibits bacterial dihydropteroate synthase, interfering with folic acid synthesis |
| Route Of Administration | Oral and injectable |
| Intended Dosage Forms | Tablets, capsules, granules, oral liquids/suspensions and injectable formulations |
| Assay | 99.0% to 101.0% on dried basis |
| Storage Conditions | Store in a tightly closed container, protected from light, in a cool and dry place |
As an accredited Sulphamethoxypyridazine base Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in double polyethylene-lined fibre drums, 25 kg net per drum, moisture-proof sealed, suitable for oral and injectable pharmaceutical formulations. |
| Container Loading (20′ FCL) | 20′ FCL of Sulphamethoxypyridazine base Pharma Grade API, securely packed in sealed drums for oral and injectable pharmaceutical formulations. |
| Shipping | Shipment handled in sealed, moisture-protected drums or double polyethylene-lined containers, labeled as pharmaceutical API. Keep dry, away from direct sunlight and heat. Valid COA and safety data sheet accompany shipment. Transport via temperature-controlled or ambient, non-hazardous cargo with secure cartons to prevent damage during transit. |
| Storage | Store Sulphamethoxypyridazine base Pharma Grade API in a tightly closed, well-sealed container, protected from light, moisture, and heat. Keep at controlled room temperature (20–25°C) in a cool, dry, well-ventilated area, away from incompatible materials. Ensure container remains closed when not in use to preserve stability, purity, and suitability for oral and injectable dosage forms. |
| Shelf Life | Shelf life: 2 years when stored in original tightly closed container, protected from light, heat, and moisture, at room temperature. |
Direct compression screening of sulphamethoxypyridazine base at API loadings above 65% w/w produces tablets with pronounced capping and lamination tendencies, attributable to the crystalline API's high elastic recovery and low plasticity index. The preferred manufacturing route for immediate-release oral tablets therefore employs wet granulation in a high-shear granulator (GEA PMA 300 or equivalent) using purified water as the granulation liquid, with polyvinylpyrrolidone K30 at 2.0–5.0% w/w of the final core mass dissolved to form the binder solution. Granulation end-point is determined by impeller torque and product temperature (22–28°C), followed by fluid bed drying (Glatt GPCG 30 or equivalent) at inlet air temperature 55–65°C until loss-on-drying of the dried granules measures 1.5–2.5% w/w by halogen moisture analyzer. Dry milling through a conical mill fitted with a 1.0–1.5 mm rasping screen and 1500–2500 rpm rotor speed yields granules with Carr index 18–22% and Hausner ratio 1.18–1.25, suitable for rotary tablet compression at 30–60 rpm turret speed on a Korsch XL 400 or Fette 3090i press. Compression force of 8–15 kN across a 13 mm round flat-faced beveled-edge tooling set produces cores with hardness 80–120 N measured by a Schleuniger hardness tester and friability ≤0.8% after 100 revolutions in a Pharmatron friabilator. The core formulation typically contains the API at 55–75% w/w, lactose monohydrate or microcrystalline cellulose PH102 at 15–30% w/w, croscarmellose sodium or sodium starch glycolate at 2.0–4.0% w/w, PVP K30 at 2.0–5.0% w/w, and magnesium stearate at 0.5–1.5% w/w added by final blending for 3–5 minutes in a bin blender at 12–15 rpm. The pharmaceutical quality framework comprising USP ‹711› Dissolution Apparatus 2 (paddle, 50–75 rpm, 900 mL medium) and USP ‹905› Uniformity of Dosage Units applies to each production batch, with dissolution acceptance criteria of Q = 75% at 45 minutes in 0.1 N hydrochloric acid or pH 6.8 phosphate buffer depending upon the target regulatory submission. In-process control for blend uniformity is performed per 21 CFR 211.110(a) using near-infrared spectroscopy or stratified sample assay with acceptance limits of 90.0–110.0% label claim and relative standard deviation ≤5.0%. Elemental impurity testing follows ICH Q3D (R2) with daily intake limits for Class 1 elements (As, Cd, Hg, Pb) assessed against the maximum daily dose. Tablet core weight for a 500 mg strength product falls within 670–830 mg, with the final dosage form delivered as uncoated scored tablets or film-coated tablets using an aqueous hydroxypropyl methylcellulose coating system applied in a perforated side-vented pan coater (Glatt Coater GC 750 or equivalent) to a weight gain of 2.0–4.0% w/w. Terminal finished product types include 250 mg and 500 mg sulphamethoxypyridazine tablets, marketed as antibacterial monotherapy for urinary tract and respiratory tract infections where regional prescribing patterns retain long-acting sulfonamides.
Encapsulation of sulphamethoxypyridazine base into hard gelatin capsules requires particle size control because milled API with a median particle size below 75 µm exhibits cohesive flow behavior and bridging in the hopper of volumetric capsule filling equipment. The API is blended with lactose monohydrate (spray-dried grade) or mannitol at 30–45% w/w, the sulphamethoxypyridazine base comprising 40–60% w/w of the fill mass, together with croscarmellose sodium 3.0–5.0% w/w, colloidal silicon dioxide 0.5–1.0% w/w, and magnesium stearate 0.5–1.0% w/w by total blend weight. Sieving of the API and major excipients through a 30–40 mesh (approximately 425–600 µm aperture) stainless steel sieve precedes blending in a bin blender at 12–15 rpm for 15–20 minutes, with lubricant added separately for the final 3–5 minutes to minimize shear-induced hydrophobic film formation on the sulfonamide crystal surfaces. The blend is charged to a dosing disc or dosator-type capsule filling machine (MG2 Compact 8 or Bosch GKF 1500) operating at 8,000–15,000 capsules/hour for size 0 or size 00 hard gelatin capsules. Fill weight control is achieved through automated weight checking with rejection of capsules outside ±5.0% of target fill weight, and process capability is assessed using USP ‹905› content uniformity requirements with an acceptance value (AV) of ≤15.0. Dissolution testing per USP ‹711› employs Apparatus 1 (basket, 100 rpm) or Apparatus 2 (paddle, 50 rpm) in 900 mL of 0.1 N hydrochloric acid, with a Q value of 75% at 45 minutes as a common specification. Compliance with ICH Q3D (R2) for elemental impurities and USP ‹467› for residual solvents is verified on the API before release for encapsulation, and the finished product is tested for microbial limits per USP ‹61› and ‹62›. Terminal dosage forms include 250 mg and 500 mg hard gelatin capsule presentations for oral administration, supplied in PVC/PVdC/aluminum blister packs or HDPE containers with desiccant.
Sulphamethoxypyridazine base is practically insoluble in purified water (approximately 0.15–0.30 mg/mL at 25°C), which dictates that oral granules for reconstitution into suspension are manufactured as sugar-based or sorbitol-based dry blends that generate a uniformly dispersed slurry only upon addition of water at the point of dispensing. The granule formulation is designed to deliver 250 mg of API per 5 mL of reconstituted suspension, with the API incorporated at 5–10% w/w of the total dry granule mass. Excipients include sucrose or sorbitol as the primary bulking and sweetening agent at 60–75% w/w, xanthan gum or sodium carboxymethylcellulose as suspending agent at 0.5–2.0% w/w, sodium benzoate or potassium sorbate as antimicrobial preservative at 0.1–0.2% w/w, citric acid monohydrate as buffering agent at 0.5–1.5% w/w, and a pharmaceutically acceptable flavoring system at 0.1–0.5% w/w. Granulation is performed in a high-shear granulator or fluid bed granulator (Glatt GPCG 30 top-spray configuration) using an aqueous binder solution of PVP K30 at 2.0–4.0% w/w, with inlet air temperature 60–70°C and product temperature maintained below 40°C to prevent thermochromic degradation of the sulfonamide, which is known to undergo light-accelerated and heat-accelerated discoloration. The dried granules are sieved through an oscillating granulator with a 1.2–1.5 mm screen and filled into unit-dose sachets using a form-fill-seal machine or into amber glass bottles with a desiccant-lined closure and a recalibration-free dropper or measuring cup. Reconstitution testing per USP ‹698› verifies deliverable volume, and sedimentation volume after 24 hours of standing is assessed as a suspension quality attribute. Preservative effectiveness is established through USP ‹51› Antimicrobial Effectiveness Testing against Staphylococcus aureus, Escherichia coli, Pseudomonas aeruginosa, Candida albicans, and Aspergillus brasiliensis, with the acceptance criterion that bacterial counts decline by at least 1.0 log₁₀ within 7 days and fungal counts show no increase from the initial count. The finished granules are tested for content uniformity per USP ‹905› on the unit-dose sachets and for moisture content by USP ‹921› Karl Fischer titration with a specification of ≤2.0% w/w. Terminal product types include 250 mg/5 mL oral suspension granules in single-dose sachets and multidose bottle presentations for pediatric and geriatric patients with dysphagia.
The conversion of sulphamethoxypyridazine base into a sterile injectable dosage form is constrained by the API's negligible aqueous solubility at physiological pH and its susceptibility to precipitation under acidic conditions. The base material is solubilized in Water for Injection by addition of 1.0 M sodium hydroxide solution with continuous stirring at 200–400 rpm in a jacketed stainless steel vessel maintained at 15–25°C, producing the water-soluble sodium salt via deprotonation of the sulfonamide nitrogen. The target concentration of sulphamethoxypyridazine as sodium salt equivalent ranges from 100–250 mg/mL expressed as base, corresponding to 10–25% w/v of the formulation. Mannitol is added as a bulking agent at 2.0–5.0% w/v to provide a crystalline lyo-cake matrix, and the pH is adjusted with 1.0 M hydrochloric acid to a final value of 9.0–9.8, which is selected because below pH 8.5 the free base precipitates as insoluble crystalline sulphamethoxypyridazine and above pH 10.5 accelerated hydrolytic cleavage of the sulfonamide linkage becomes measurable by HPLC. The solution is pre-filtered through a 0.45 µm polyethersulfone membrane and then sterile-filtered through two 0.22 µm polyvinylidene fluoride membrane filters in series, with filter integrity testing performed by bubble point and diffusive flow methods per USP ‹71› Sterility Tests and EU GMP Annex 1 (2022 revision) section 8.87 on filter integrity. Aseptic filling into Type I borosilicate glass vials (2R, 5R, or 10R) is conducted in a Grade A/ISO 5 environment under Grade B/ISO 7 background using a peristaltic pump with disposable tubing and a fill volume of 2.0–20.0 mL depending upon final label claim. The filled vials are partially stoppered with bromobutyl lyophilization stoppers and transferred to a freeze dryer with shelf temperature control. The lyophilization cycle is designed around the collapse temperature of the mannitol–sodium sulphamethoxypyridazine matrix, which is measured by freeze-drying microscopy; typical collapse onset occurs between -30°C and -25°C, dictating a primary drying shelf temperature of -25 to -20°C at a chamber pressure of 100–200 mTorr (13–27 Pa). Freezing is conducted at -40 to -45°C for 3–5 hours, followed by primary drying for 18–30 hours and secondary drying at +25 to +35°C for 6–12 hours, with product temperature monitored via thermocouples and Pirani gauge versus capacitance manometer readings used to detect the end of primary drying. The finished lyophilized cake is inspected for particulate matter per USP ‹788› Particulate Matter in Injections (light obscuration method) and USP ‹790› Visible Particulates in Injections, tested for bacterial endotoxins per USP ‹85› with a limit of ≤0.25 EU/mg of sulphamethoxypyridazine, and subjected to sterility testing per USP ‹71› using the membrane filtration method. Residual moisture in the cake is determined by USP ‹921› Karl Fischer titration with a specification of ≤2.5% w/w. Photostability data for the reconstituted solution indicate significant degradation under ICH Q1B light exposure (overall illumination 1.2 million lux-hours, near-UV energy 200 watt-hours/m²), so the final container is an amber vial, and the product is stored protected from light at 15–25°C. Terminal dosage forms include 500 mg and 1 gram lyophilized powder for solution for injection, reconstituted with Sterile Water for Injection to a concentration of 100–250 mg/mL for slow intravenous infusion or deep intramuscular injection. Published data for this specific configuration is limited, and formulation development batches should prospectively validate the lyophilization cycle with product temperature mapping and residual moisture data generated on the actual freeze dryer to be used for commercial production.
Sulphamethoxypyridazine base is formulated into large oblong veterinary boluses for oral administration to cattle, sheep, and goats, where the dose ranges from 30–60 mg/kg body weight depending on the infectious indication and regional prescribing guidelines. Bolus compression differs from conventional tablet compression in that the API is dry granulated by roller compaction (Alexanderwerk WP 120 or Fitzpatrick CCS 220) because wet granulation of high-dose sulfonamide formulations produces over-granulated ribbons that break into particles with excessive fines generation, reducing subsequent die filling efficiency. The API fraction in the bolus core typically spans 25–50% w/w, with microcrystalline cellulose or dicalcium phosphate dihydrate as filler at 30–50% w/w, sodium starch glycolate at 2.0–4.0% w/w as disintegrant, and magnesium stearate at 0.5–1.0% w/w as lubricant. Compression is performed on a heavy-duty single-station or rotary tablet press designed for large tooling (oblong punches of 18–22 mm tip length and 9–12 mm tip width), with compression force calibrated to produce a crushing strength of 120–200 N measured across the bolus long axis. The disintegration test for boluses does not follow human pharmacopeial apparatus because of the size exclusion from USP ‹701›; dissolution testing is conducted instead in USP ‹711› Apparatus 2 at 75–100 rpm using 900 mL of pH 5.8 acetate buffer or dilute hydrochloric acid (0.1 N) to approximate rumen and abomasal fluid conditions. Rumen retention and dissolution are influenced by bolus density, with an acceptable density range of 1.10–1.30 g/cm³ to prevent regurgitation while allowing gradual sink into the rumen liquor. The finished bolus is tested for residual solvents per VICH GL18(R2), for related substances per VICH GL11, and for release under the veterinary medicinal product quality requirements of EU Regulation 2019/6 Article 93 and 21 CFR Part 514 where applicable. Terminal products include 500 mg, 1 gram, and 2 gram sulphamethoxypyridazine boluses, individually packed in peelable aluminum foil blisters to prevent moisture uptake, which above 60% RH causes softening and loss of mechanical integrity of the bolus core.
The combination of sulphamethoxypyridazine base and trimethoprim at a fixed 5:1 ratio (for example, 400 mg sulphamethoxypyridazine plus 80 mg trimethoprim per tablet) introduces measurable dissolution interference that does not occur in single-component formulations, because trimethoprim is a weak base with pH-dependent solubility that partitions differently from the sulfonamide across the pH range of 1.2–6.8. At pH 1.2 both actives dissolve relatively rapidly, but at pH 4.5 acetate buffer the dissolution rate of trimethoprim declines sharply while sulphamethoxypyridazine remains ionized in its sodium-form microclimate, creating a divergent release profile that necessitates formulation-level intervention. Granulation for this fixed-dose combination is performed in a high-shear granulator with an aqueous PVP K30 binder solution at 2.0–5.0% w/w, with the API fraction totaling 55–70% w/w of the core mass and filler consisting of lactose monohydrate or microcrystalline cellulose PH101 at 15–30% w/w. Disintegrant selection is critical: croscarmellose sodium at 3.0–5.0% w/w provides rapid tablet disintegration (less than 5 minutes in purified water) and creates microenvironments that partially compensate for the trimethoprim dissolution lag, whereas sodium starch glycolate at equivalent levels produces slower disintegration (10–15 minutes) and fails to achieve the Q value for trimethoprim at early time points in dissolution testing. Compression is performed on a rotary tablet press with 13 mm round tooling at 8–15 kN force, targeting core hardness 70–110 N, and the cores are film-coated with an aqueous HPMC system to 2.0–3.0% w/w weight gain. Dissolution testing follows USP ‹711› Apparatus 2 at 50 rpm in 900 mL of 0.1 N hydrochloric acid (pH 1.2) for both analytes, with acceptance criteria of not less than 75% dissolved at 45 minutes for sulphamethoxypyridazine and not less than 70% for trimethoprim at the same time point, with both analytes quantified by a validated HPLC method using a C18 column and UV detection at 254 nm. Additional dissolution profiling in pH 4.5 acetate buffer and pH 6.8 phosphate buffer is recommended to characterize the formulation across the gastrointestinal pH gradient, and the European Pharmacopoeia 11.0 general chapter 2.9.3 requires dissolution profile comparison (f₂ similarity factor) when proposing scale-up changes. Related substances testing must resolve trimethoprim degradation products, particularly the benzyl pyrimidine oxidative derivatives, using HPLC gradient elution with photodiode array detection per Ph.Eur. 2.2.29. The combination tablet is governed additionally by USP ‹905› for content uniformity of both actives and ICH Q3D (R2) for elemental impurities applied to the blended API-plus-excipient matrix. Terminal product types include 400 mg/80 mg and 500 mg/100 mg fixed-dose combination tablets, positioned primarily in veterinary and select human regional markets where sulphamethoxypyridazine–trimethoprim combinations remain part of national formularies. Operational incompatibility is noted with highly alkaline granulated systems: maintaining granulation moisture above 6.0% w/w during high-shear mixing causes localized hydrolysis of trimethoprim and discoloration of the sulfonamide, so tray drying or fluid bed drying must reduce loss-on-drying to 1.5–2.5% w/w within 45–60 minutes immediately after granulation to prevent this degradation pathway.
| Formulation Variable | Variant A (Low Disintegrant) | Variant B (Mid Disintegrant) | Variant C (High Disintegrant) |
|---|---|---|---|
| Croscarmellose sodium (% w/w) | 1.0% | 3.0% | 5.0% |
| API (% w/w) | 70.0% | 65.0% | 60.0% |
| Lactose monohydrate (% w/w) | 24.0% | 26.5% | 29.0% |
| Core hardness (N) | 95–115 N | 85–110 N | 75–95 N |
| Disintegration time (min) | 14–18 min | 6–9 min | 3–5 min |
| Dissolution at 45 min (%), USP Apparatus 2, 0.1 N HCl, 50 rpm | 68–74% | 86–93% | 94–99% |
| Friability (% w/w after 100 revolutions) | 0.55–0.75% | 0.40–0.60% | 0.45–0.70% |
| Dosage Form | Compendial Standard | Regulatory Reference | Test Method Designation |
|---|---|---|---|
| Oral tablet | USP 42–NF 37 | 21 CFR 211.110(a) | USP ‹711› Dissolution, Apparatus 2 |
| Oral tablet | USP 42–NF 37 | ICH Q3D (R2) | USP ‹905› Uniformity of Dosage Units |
| Capsule | USP 42–NF 37 | ICH Q3D (R2) | USP ‹711› Dissolution, Apparatus 1 or 2 |
| Capsule | USP 42–NF 37 | 21 CFR 211.122 | USP ‹61›/‹62› Microbial Limits |
| Oral granules | Ph.Eur. 11.0 | ICH Q3D (R2) | USP ‹698› Deliverable Volume |
| Oral granules | Ph.Eur. 11.0 | 21 CFR 211.166 | USP ‹51› Antimicrobial Effectiveness |
| Sterile injectable | Ph.Eur. 11.0 | EU GMP Annex 1 (2022) | USP ‹71› Sterility Tests |
| Sterile injectable | Ph.Eur. 11.0 | EU GMP Annex 1 §8.87 | USP ‹85› Bacterial Endotoxins ≤0.25 EU/mg |
| Sterile injectable | Ph.Eur. 11.0 | ICH Q3D (R2) | USP ‹788›/‹790› Particulate Matter |
| Veterinary bolus | Ph.Eur. 11.0 (veterinary monograph) | VICH GL18(R2) | USP ‹711› Dissolution, Apparatus 2 |
| Veterinary bolus | Ph.Eur. 11.0 (veterinary monograph) | EU Regulation 2019/6 Article 93 | Residual moisture USP ‹921› Karl Fischer |
| Fixed-dose combination tablet | USP 42–NF 37 | ICH Q3D (R2) | USP ‹711› Dissolution, dual-analyte HPLC |
| Fixed-dose combination tablet | Ph.Eur. 11.0 | Ph.Eur. 2.9.3 | USP ‹905› Uniformity of Dosage Units |
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Sulphamethoxypyridazine base is a non-sterile, pharma-grade sulfonamide active pharmaceutical ingredient supplied for the manufacture of tablets, capsules, granules, and injectable finished dosage forms. The compound is identified by CAS 80-35-3, molecular formula C11H12N4O3S, and molecular weight 280.30 g/mol; the pharmacopoeial designation is sulfamethoxypyridazine. The base form contains an aromatic amine and a weakly acidic sulfonamide centre, and its antibacterial action is attributed to competitive inhibition of dihydropteroate synthase, thereby blocking bacterial folate synthesis. Two physical grades are typically controlled for downstream use: an unmicronized base for wet granulation and a micronized base for direct compression or low-dose capsule filling. The product is differentiated from sulfadiazine, sulfamethoxazole, and sulfadimethoxine by the presence of a 6-methoxypyridazinyl substituent, which increases lipophilicity and alters elimination kinetics relative to shorter-acting sulfonamides. The base is not a finished dosage form; it requires further processing under ICH Q7 or equivalent current good manufacturing practice.
Sulfamethoxazole contains an isoxazole ring and is commonly co-formulated with trimethoprim. Sulfadiazine is a smaller, more hydrophilic sulfonamide with faster renal elimination in many species. Sulfadimethoxine contains dimethoxy pyrimidine substitution and is recognised for long-acting behaviour in veterinary use. Sulphamethoxypyridazine occupies an intermediate to long-acting pharmacokinetic position, and the methoxypyridazinyl group changes wetting, dissolution, and permeability behaviour in aqueous media. The base exhibits pH-dependent solubility because the sulfonamide nitrogen and the aromatic amine can participate in acid-base equilibria. Compared with the sodium salt, the base has lower water solubility and higher lipophilicity, which can reduce moisture uptake during dry processing but may require pH adjustment or a co-solvent strategy for injectable manufacture. Published comparative dissolution data for this specific compendial base under modern cGMP conditions are limited; therefore, intrinsic dissolution should be characterised by a flow-cell or rotating-disc method before the granulation route is fixed.
During tablet and capsule manufacture, the base is normally pre-screened through a 0.5 mm or 0.8 mm sieve and then blended in a bin blender or plough mixer to reduce agglomerates. Because the base is hydrophobic relative to common water-soluble excipients, aqueous wet granulation can improve active distribution, but the granulation endpoint is influenced by water addition rate and impeller load in a high-shear mixer. For high-shear wet granulation, the water quantity is determined product-specifically by torque or power draw, and the wet mass is milled before drying. Fluid-bed drying inlet air is commonly held at 50–65 °C for heat-sensitive sulfonamide granulations, but the drying endpoint is defined by loss on drying rather than time alone. After drying, granules are milled to the target particle-size distribution and blended with disintegrant, lubricant, and glidant. The final blend is compressed on a rotary tablet press to achieve friability below 1.0% and disintegration according to the applicable pharmacopoeial method. For capsules, the micronized base can be filled into hard gelatin or hypromellose capsules after dry pre-mixing; however, at high active load, roller compaction is used to improve flow and reduce segregation. Roll pressure and gap width should be set so that ribbons retain compressibility and do not create excessive fines.
Release testing for the pharma-grade base typically includes appearance, identification by infrared absorption and chromatographic retention, assay on the dried basis, loss on drying, residue on ignition, related substances, residual solvents, and elemental impurities. Particle-size distribution is controlled by laser diffraction according to ISO 13320-1:2020, with product-specific D10, D50, and D90 values selected for the intended dosage form. Published product-specific particle-size ranges for this API are limited. Polymorphic form is monitored by X-ray powder diffraction and should match the approved reference pattern. The base is sensitive to humidity; storage below 60% relative humidity and protection from light are recommended to limit hydrolysis and photodegradation. For injectable use, the non-sterile base must be supported by additional bioburden control, and the finished injectable solution must meet bacterial endotoxin and sterility requirements appropriate to the route and maximum daily dose.
| Quality attribute | Representative control | Reference method or standard |
|---|---|---|
| Description | White to off-white crystalline powder | Visual examination |
| Identification | Infrared absorption and HPLC retention time | Ph. Eur. 2.2.24, USP 197 |
| Assay, dried basis | 98.0–102.0% w/w | HPLC |
| Loss on drying | ≤0.5% w/w | Drying at 105 °C |
| Residue on ignition | ≤0.1% w/w | Compendial muffle furnace method |
| Related substances, total | ≤1.0% | HPLC, area normalisation |
| Related substances, unspecified | ≤0.10% | HPLC, area normalisation |
| Residual solvents | Class 1 below compendial limits; other solvents risk-based | ICH Q3C, USP 467, Ph. Eur. 2.4.24 |
| Elemental impurities | Risk-based, per intended use | ICH Q3D, USP 232/233, Ph. Eur. 2.4.8 |
| Particle size | D10, D50, D90 report or agreed range | ISO 13320-1:2020 |
| Polymorphic form | Consistent with reference XRPD pattern | XRPD |
| Microbial enumeration, oral grade | Total aerobic microbial count ≤10² CFU/g; total combined yeasts and moulds ≤10¹ CFU/g | Ph. Eur. 2.6.12, USP 61 |
| Bacterial endotoxins, injectable use | Limit derived from maximum dose and route | USP 85, Ph. Eur. 2.6.14 |
The tabulated values are representative of current sulfonamide base monographs and manufacturer release specifications. The filed specification may differ, and the exact acceptance criteria must be confirmed against the applicable regulatory dossier and current pharmacopoeial monograph.
Sterile injectable manufacture from the base API imposes a different control hierarchy. The base is non-sterile and is not intended for direct use without terminal sterilisation or aseptic processing. The weakly acidic sulfonamide nitrogen permits dissolution in alkaline aqueous media, but the aromatic amine can undergo oxidative discolouration if dissolved oxygen is not controlled. Nitrogen blanketing and light-protected vessels are therefore used when preparing injectable solutions. The solution is passed through a sterilising-grade membrane with a pore size of 0.22 µm, but filter compatibility must be confirmed because low-concentration aromatic amine solutions can adsorb to certain filter polymers and reduce assay recovery. For terminal sterilisation, a standard autoclave cycle at 121 °C for 15 minutes may be evaluated; however, forced degradation studies are required to demonstrate that the impurity profile remains within specification. If terminal sterilisation is not feasible, aseptic processing is required with environmental monitoring and media fill acceptance according to current GMP. The injectable dosage form should be stored in amber glass vials and protected from light unless photostability data demonstrate otherwise.
For oral solid dosage forms, a coarser particle distribution may be preferred because it reduces surface area and improves flow; however, for low-dose tablets and capsules, a micronized grade may be required to achieve content uniformity. This creates a process conflict: excessive micronization can increase electrostatic charging, lower bulk density, and promote sticking or non-uniform filling. The selected grade must therefore be matched to the dosage form and the specified manufacturing route. For injectable use, particle size becomes less relevant once the base is dissolved, but bioburden and endotoxin burden become critical. A nominally “pharma-grade” base is not automatically acceptable for injectable manufacture unless the supplier has controlled microbial enumeration and endotoxin at the API stage. When the same base is intended for oral and injectable development, the stricter injectable bioburden limit governs. Process analytical technology can monitor blend uniformity in real time, but published data for this specific API under PAT-based control are limited.
At ambient storage, the base should be kept in tightly closed, light-resistant containers under nitrogen or dry air. The material is incompatible with strong oxidising agents and should not be exposed to high-humidity environments for extended periods. Pre-drying may be required when ambient relative humidity exceeds 60%, especially for micronized grade used in direct compression. Avoid processing with unbuffered strongly acidic or strongly alkaline solutions unless the resulting impurity profile has been demonstrated to remain within specification. The oral and injectable formulations should include appropriate control of dose, particle size, and degradation products because the safety profile of sulfonamides includes recognised risks of hypersensitivity, crystalluria, and blood dyscrasias in susceptible patients. Published data for this specific configuration in modern continuous manufacturing lines are limited; therefore, process validation studies should be designed to capture batch-to-batch variability in particle size, moisture, and bulk density.