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Analgin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Analgin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 380814
    Product Name Analgin Pharma Grade API for Tablet/Capsule/Granule/Injection (Oral and Injectable)
    Active Substance Metamizole Sodium (Analgin / Dipyrone)
    Api Grade Pharma Grade / Pharmaceutical Grade
    Molecular Formula C13H16N3NaO4S·H2O
    Molecular Weight 351.36 g/mol (monohydrate)
    Cas Number 5907-38-0 (monohydrate); 68-89-3 (anhydrous)
    Chemical Classification Pyrazolone derivative
    Therapeutic Category Analgesic and antipyretic
    Mechanism Type Non-opioid analgesic with antipyretic and spasmolytic activity
    Physical Form White or slightly yellowish crystalline powder
    Solubility Freely soluble in water; soluble in ethanol; practically insoluble in ether
    Assay Content 99.0% to 101.0% on dried basis
    Route Of Administration Oral and injectable
    Intended Dosage Forms Tablet, capsule, granule, and injection
    Storage Conditions Store in a well-closed container, protected from light, moisture, and heat
    Quality Standard Meets pharmaceutical pharmacopoeia requirements (e.g., Ph.Eur./BP/CP)

    As an accredited Analgin 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 & Storage
    Packing Supplied as 25 kg net in sealed polyethylene bags inside fiber drums, with tamper-evident closure and complete product labeling.
    Container Loading (20′ FCL) 20′ FCL loading of Analgin Pharma Grade API: sealed, palletized drums, secured and protected for oral/injectable tablet, capsule, granule formulations.
    Shipping Analgin Pharma Grade API ships in sealed, moisture-proof polyethylene-lined drums, protected from light and contamination. Transport occurs under ambient, dry conditions in clean ventilated vehicles. Shipment includes full documentation—COA, MSDS, batch number, and regulatory compliance for oral and injectable dosage forms. Customs and pharmaceutical logistics standards are strictly followed to ensure product integrity.
    Storage Store Analgin Pharma Grade API in tightly closed, moisture-proof containers, away from direct sunlight, heat, and humidity. Keep in a cool, dry, well-ventilated area at controlled room temperature (15–30°C). For injectable grade, maintain strict hygiene and avoid contamination. Store separately from oxidizing agents and incompatible substances. Follow first-expiry-first-out rotation to preserve potency and shelf life.
    Shelf Life Analgin API shelf life: 36 months when stored in airtight containers, kept cool, dry, and protected from light.
    Application of Analgin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Received metamizole sodium monohydrate with particle-size distribution D50 ≤ 150 µm and D90 ≤ 250 µm is directly suited for blending with microcrystalline cellulose PH102 at API loadings of 70–85% w/w only after moisture sorption is confirmed below 2.0% w/w by Ph. Eur. 2.2.32. The direct compression formulation is constrained by the brittle fracture behaviour of the API at compaction pressures above 150 MPa; therefore the lubricant system is limited to 0.5–1.0% w/w magnesium stearate blended separately through a 0.5 mm screen for 3–5 min in a 600 L bin blender. A representative batch uses 75.0% w/w metamizole sodium monohydrate, 14.5% w/w microcrystalline cellulose PH102, 5.0% w/w crospovidone type A, 3.0% w/w sodium starch glycolate, 0.5% w/w colloidal silicon dioxide, and 1.0% w/w magnesium stearate. Compression on a 45-station rotary tablet press with 12 mm round flat-faced bevel-edge punches uses pre-compression 5–8 kN, main compression 14–20 kN, turret speed 35–55 rpm, and force-feeder paddle speed 25–35 rpm; tablet hardness is held at 85–115 N, thickness 3.8–4.2 mm, friability ≤0.8% by Ph. Eur. 2.9.7, and disintegration ≤15 min by Ph. Eur. 2.9.1. In-process uniformity is verified by Ph. Eur. 2.9.40 at three intervals per batch; dissolution is tested in 900 mL deaerated water at 37 ± 0.5 °C, paddle 50 rpm, with sampling at 15 min, 30 min, and 45 min and a product-specific Q value of ≥80% at 30 min under ICH Q6A. Batch-to-batch variance in API bulk density between 0.45 g/mL and 0.60 g/mL is a known production bottleneck on high-speed presses; loss-in-weight feeder control and forced feeder paddle adjustment are required to prevent fill weight drift beyond ±3%. Compliance for this oral solid dosage route applies the current European Pharmacopoeia monograph for metamizole sodium monohydrate, ICH Q3D Table 1 element limits based on a 10 g/day maximum oral intake, ICH Q3C for any residual processing solvents, and EU GMP Part II / ICH Q7 for API handling. Terminal dosage type is a non-coated or aqueous film-coated tablet of 500 mg label claim, packed in PVC/aluminium or PA/Al/PVC blisters.

    Why Does Wet Granulation Reduce Capping Defects in 500 mg Metamizole Sodium Tablets?

    Metamizole sodium tablets formulated above 70% w/w by direct compression often display capping at hardness values above 100 N, caused by elastic recovery after decompression and low tensile strength of the compact. Moving to wet granulation changes the compaction mechanism by embedding API particles in a porous granule network. The formulation addition ratio for wet granulation is set at 55–68% w/w metamizole sodium monohydrate, 15–25% w/w lactose monohydrate 200M, 5–10% w/w maize starch, 2–4% w/w povidone K30 binder dissolved in purified water, 2–5% w/w croscarmellose sodium intra-granular, 0.5–1.0% w/w colloidal silicon dioxide, and 0.5–1.0% w/w magnesium stearate extra-granular. The high-shear wet granulation process uses a 600 L top-drive granulator with impeller speed 150–200 rpm, chopper 1500–2500 rpm, atomized purified water addition of 8–15% w/w at 0.5–1.0 kg/min, and a kneading time after water addition of 90–240 s until power consumption increases by 15–25% over the dry blend baseline. Overwetting above 15% w/w water produces large agglomerates that survive 1.0 mm screening and generate tablet hardness variability across the press. Wet granules are dried in a fluid-bed dryer with inlet air 55–70 °C and product temperature not exceeding 45 °C; final moisture is controlled at 1.5–2.5% w/w by Ph. Eur. 2.2.32. Dried granules are screened through 1.0 mm and mixed with extra-granular disintegrant. Tableting on a 45-station rotary press uses main compression 12–18 kN, hardness 120–180 N, friability ≤0.5%, and disintegration ≤15 min. Dissolution testing per Ph. Eur. 2.9.3 with 900 mL water, paddle 50 rpm, and acceptance ≥80% in 30 min applies; uniformity of dosage units follows Ph. Eur. 2.9.40. Compliance includes ICH Q3A and ICH Q3B degradation product thresholds calculated for a maximum daily intake of 4 g/day, ICH Q3D Table 1 elemental impurity limits, ICH Q1A(R2) stability for moisture-sensitive primary packaging, and current European Pharmacopoeia assay requirements. Published degradation kinetics data for aqueous granulation hold time of metamizole sodium beyond 6 h is limited; therefore, hold time studies are conducted as part of ICH Q1A(R2) process validation. Terminal dosage type is film-coated tablet 500 mg label claim, with aqueous film coating applied at 3–4% w/w weight gain.

    Roller-compacted metamizole sodium granulate for hard capsule filling is produced when the batch size or regional packaging format favours two-piece capsules over tablets. The internal granulation uses 70–80% w/w metamizole sodium monohydrate, 10–18% w/w lactose monohydrate or pregelatinized starch, 3–5% w/w sodium starch glycolate, 1–2% w/w colloidal silicon dioxide, and 0.5–1.0% w/w magnesium stearate. Ribbon compaction on a 220K roller compactor with roll surface speed 5–15 rpm, hydraulic pressure 80–120 bar, and ribbon density 1.1–1.3 g/cm³ yields flakes that are milled through a 1.0 mm screen with an oscillating sieve mill. The milled granulate is passed through a 0.8 mm screen before final blending in a 400 L bin blender at 10 rpm for 20 min; bulk density is controlled at 0.55–0.65 g/mL and Carr index at 20–25 to prevent weight variation on dosator filling. Encapsulation is performed on a dosator-type capsule filler at 50,000–100,000 capsules/h using size 0 hard gelatin or HPMC capsules; fill weight 600–700 mg delivers 500 mg metamizole sodium per unit. Dosator capsule fillers show weight variation when granulate Carr index exceeds 25; hopper agitation and granulate temperature below 25 °C are used to limit electrostatic adhesion. Process controls include in-process fill weight checks at 15-min intervals, rejection of capsules outside ±5% of target fill weight, and metal detection at 0.3 mm ferrous sensitivity. Compliance includes Ph. Eur. 2.9.40 for uniformity of dosage units, Ph. Eur. 2.9.1 for disintegration, Ph. Eur. 2.9.3 dissolution in 900 mL water, ICH Q3D Table 1, ICH Q3C, and ICH M7 for mutagenic impurities; nitrosamine risk is controlled by testing N-nitrosodimethylamine and N-nitrosodiethylamine below regulatory interim limits. Terminal dosage type is hard capsule 500 mg, packed in PVC/PVDC/aluminium blisters or HDPE bottles with desiccant.

    Water-Soluble Oral Granules in Single-Dose Sachets Under High-Daily-Dose Degradation Thresholds

    Single-dose sachets containing metamizole sodium oral granules are formulated for rapid reconstitution in water, requiring a water-soluble carrier and strict moisture control. The addition ratio is 75–90% w/w metamizole sodium monohydrate, 5–15% w/w sucrose or sorbitol, 1–3% w/w citric acid, 0.5–1.0% w/w sodium saccharin, and 0.1–0.5% w/w flavour; the total fill mass per sachet is 1.0–2.0 g to deliver 500 mg metamizole sodium. Dry granulation by roller compaction is preferred over wet granulation because residual water above 1.5% w/w in the sachet leads to caking and reduced dispersion. The roller compactor operates at ribbon density 1.0–1.3 g/cm³, mill screen 0.8–1.25 mm, and the final granulate moisture is confirmed below 1.5% w/w by Ph. Eur. 2.2.32. Filling is performed on a vertical form-fill-seal sachet machine with nitrogen flush; heat-seal temperature 135–155 °C for aluminium-polyethylene laminate, residual oxygen ≤5% in headspace, and seal width ≥8 mm are monitored. Production experience shows that seal failures increase when powder dusting in the seal area exceeds 50 mg/cm², requiring vacuum extraction and periodic seal jaw cleaning. Uniformity of mass for single-dose granules follows Ph. Eur. 2.9.5; uniformity of content is verified by Ph. Eur. 2.9.40 when justified. Dispersion is evaluated by adding one sachet to 100 mL water at 25 ± 2 °C with stirring 50 rpm; complete dispersion occurs within 3 min because of the water-soluble formulation. Compliance includes ICH Q3B thresholds recalculated for a 4 g/day maximum daily intake, ICH Q3D Table 1 elemental impurities, and EU GMP Part II / ICH Q7. Terminal dosage type is single-dose oral granules in sachet, 500 mg.

    Oral solid routeAPI loadingCritical process controlEndpoint dosagePrimary standards
    Direct compression70–85% w/wMain compression 14–20 kN; hardness 85–115 NTablet 500 mgPh. Eur. 2.9.7, 2.9.1, 2.9.40
    Wet granulation55–68% w/wWater addition 8–15% w/w; hardness 120–180 NFilm-coated tablet 500 mgPh. Eur. 2.9.3, 2.9.40, ICH Q3B
    Roller compaction for capsules70–80% w/wRibbon density 1.1–1.3 g/cm³; Carr index 20–25Hard capsule 500 mgPh. Eur. 2.9.1, 2.9.40, ICH M7
    Single-dose sachet granules75–90% w/wResidual oxygen ≤5%; moisture <1.5% w/wSachet granules 500 mgPh. Eur. 2.9.5, 2.9.40, ICH Q3B

    When Terminal Moist-Heat Sterilization of Metamizole Sodium Injection Demands Impurity Re-Profiling

    Injectable metamizole sodium is manufactured as a 500 mg/mL aqueous solution, corresponding to 50% w/v API concentration. The formula uses water for injection q.s., hydrochloric acid or sodium hydroxide for pH adjustment to 6.0–7.0, and, where terminal sterilization is selected, nitrogen blanketing to reduce oxidative degradation; some registered formulations include sodium metabisulfite at 0.01–0.05% w/v as oxygen scavenger, but sulfur exposure must be declared due to allergic cross-reactivity in patients. The compounding vessel is jacketed at 15–25 °C, and the API is added under vacuum to prevent foam; dissolution is confirmed by refractive index or density checks. Filtration passes the solution through a 0.45 µm prefilter and a 0.22 µm polyvinylidene fluoride sterilizing filter into Type I glass ampoules of 2 mL or 5 mL capacity. Terminal sterilization in a saturated steam autoclave at 121 °C for 15 min with F0 ≥8 is applied only after the degradation product profile is re-profiled; if any unidentified degradation product exceeds the ICH Q3B reporting threshold for the 4 g/day injectable maximum daily dose, aseptic processing without terminal heat is required. Ampoule neck cracking occurs when autoclave pressure equalization exceeds 2.0 bar during cooling; therefore, pressure ramp control and post-autoclave visual inspection for container integrity are mandatory. The filled ampoule solution is inspected for visible particles by Ph. Eur. 2.9.20, sub-visible particles by Ph. Eur. 2.9.19, bacterial endotoxins by Ph. Eur. 2.6.14 with the limit derived from the K/M calculation for the maximum bolus dose and route of administration, and sterility by Ph. Eur. 2.6.1. Compliance includes ICH Q3C for residual solvents, ICH Q3D Table 1 for elemental impurities using parenteral permitted daily exposures, and current European Pharmacopoeia parenteral preparation requirements. Published data for terminal sterilisation of metamizole sodium in ampoules across all pH conditions is limited; terminal sterilization therefore requires a product-specific degradation database before validation. Terminal dosage type is single-dose glass ampoule, 2 mL (1000 mg) and 5 mL (2500 mg) for slow intravenous or intramuscular administration.

    For veterinary drinking-water administration, metamizole sodium is supplied as a water-soluble powder or granule premix with API loading of 20–50% w/w in a carrier of lactose monohydrate or glucose monohydrate. The field dose is adjusted to 10–30 mg/kg body weight per day, and the carrier blend is diluted in drinking water at a concentration not exceeding 2 g/L to prevent precipitation and intake variability. Production uses a horizontal band blender of 500 kg working capacity, paddle speed 12–18 rpm, mixing time 15–25 min, and post-mix uniformity tested on 10 stratified samples by HPLC; coefficient of variation ≤5% is the release criterion. Segregation occurs when carrier particle size difference exceeds 100 µm; therefore carriers are pre-sieved through 0.25 mm and matched to the API particle-size distribution. The powder is sieved through 0.5 mm, and moisture is controlled below 2.0% w/w by Ph. Eur. 2.2.32 to avoid channeling in volumetric dosing pumps. Packaging into 100 g, 500 g, and 1 kg polyethylene jars or laminated foil pouches includes heat-sealed desiccant. Compliance is governed by EU GMP for veterinary medicinal products, VICH GL 18 for residual solvents, and Ph. Eur. 2.2.32 for moisture; published data for specific metamizole sodium premix stability under tropical field conditions is limited, so accelerated stability is required at 40 ± 2 °C / 75 ± 5% RH. Terminal dosage type is water-soluble powder or granule for oral administration in drinking water, supplied as 100 g, 500 g, or 1 kg packs.

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    Certification & Compliance
    More Introduction

    Analgin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a compendial-grade metamizole sodium monohydrate supplied as a white or almost white crystalline powder. The anhydrous sodium salt corresponds to CAS 68-89-3; the monohydrate contains a theoretical water equivalent of 5.13% m/m. Specification testing is aligned with the current European Pharmacopoeia monograph for metamizole sodium and uses the Ph. Eur. general methods listed in Table 1. The material is intended for immediate-release tablet, capsule, and granule manufacturing as well as for aseptic injectable solution preparation. Because the API is freely soluble in water under Ph. Eur. 5.11, downstream processing differs substantially from poorly soluble analgesic APIs. Release for solid oral dosage forms includes microbiological enumeration by Ph. Eur. 2.6.12 and 2.6.13; injectable applications additionally require bacterial endotoxins testing by Ph. Eur. 2.6.14. The typical crystal form is the monohydrate; published data for alternative polymorphic forms of this specific pharmaceutical grade is limited.

    Analgin Pharma Grade API control areas and compendial methods
    Control areaCompendial or regulatory methodDownstream relevance
    Identification by infrared absorptionPh. Eur. 2.2.24Confirms chemical identity against the reference spectrum and prevents dispense mix-ups.
    Assay and related substancesPh. Eur. 2.2.29 liquid chromatographySets potency on the dried basis and controls hydrolytic degradation products.
    Water contentPh. Eur. 2.5.12Verifies monohydrate hydration state; influences flow and recrystallization during wet granulation.
    Residual solventsPh. Eur. 2.4.24; ICH Q3CLimits volatile process solvents from synthesis and purification.
    Elemental impuritiesPh. Eur. 2.4.20; ICH Q3DControls trace metals that can catalyze oxidative colour development in solution.
    Microbial enumerationPh. Eur. 2.6.12, 2.6.13Defines oral-dose bioburden release boundaries.
    Bacterial endotoxinsPh. Eur. 2.6.14Required when the API is used for parenteral formulations.

    Because the monohydrate is hygroscopic, the API is supplied in polyethylene-lined aluminium or fibre containers with desiccant. Open handling should be limited; storage is in an airtight container protected from light as specified in the current monograph. Humidity excursions above typical pharmaceutical warehouse conditions can increase surface water and lower powder flow. When a receiving site repackages the API into intermediate bulk containers, moisture uptake is checked by Ph. Eur. 2.5.12 and the material is returned to the validated storage environment if the water content exceeds release data. The API should not be dry-heat sterilized because removal of lattice water changes the monohydrate crystal habit and can modify tablet compression behaviour.

    When Direct Compression Requires Particle-Size and Flow Control

    Direct-compression processing of this API is evaluated with reference to powder flow, compressibility, and segregation tendency. Particle-size distribution is measured by laser diffraction according to Ph. Eur. 2.9.31, and bulk and tapped density are measured by Ph. Eur. 2.9.34; the Hausner ratio calculated from these values determines whether preblending with colloidal silicon dioxide is required. On an instrumented rotary tablet press with compaction force monitored by strain-gauge punches, immediate-release batches are compressed to target disintegration time by Ph. Eur. 2.9.1 and friability by Ph. Eur. 2.9.7. Because metamizole sodium is freely soluble, dissolution under Ph. Eur. 2.9.3 is usually matrix-disintegration-controlled rather than solubility-controlled; excess lubricant can delay disaggregation. Pilot-scale tumble-blender experience indicates that segregation of the API and direct-compression fillers can occur during hopper discharge; sampling-thief blend uniformity studies by Ph. Eur. 2.9.6 are used to define sampling locations and lubrication time. For capsule filling, automatic dosator or tamping-pin machines are used after the powder blend is passed through a conical mill screen of 0.8 mm or 1.0 mm; selection depends on capsule size and target fill weight.

    In compaction simulation, the sodium-salt surface chemistry of metamizole can generate die-wall friction; instrumented single-punch simulators quantify compression, decompression, and ejection shear stress. Tablet tooling is evaluated for picking and sticking on production batches. If sticking occurs, the corrective sequence is not the addition of excessive magnesium stearate but the use of a harder granulated intermediate or a low-friction tool coating. Lubricant level is optimized by measuring tablet ejection force and disintegration time. The relationship between compression force and the resulting solid fraction is interpreted with Heckel analysis; this data is specific to the incoming particle-size distribution and monohydrate crystal habit. Powder flow is released by Ph. Eur. 2.9.36, not by angle-of-repose alone. An angle of repose above 45° in a standard funnel usually indicates the need for a glidant or a granulated intermediate, but the compendial flow method remains the release test.

    What Limits Endotoxin and Particulate Burden in Injectable Formulations?

    Parenteral dosage-form development imposes additional quality constraints on the API. The finished solution is aseptically filtered through a sterilising-grade 0.22 μm membrane and filled into Type I borosilicate glass ampoules; terminal steam sterilisation is not assumed to be compatible because aqueous metamizole sodium undergoes hydrolytic degradation and colour development at elevated temperature. Particulate contamination of the finished product is measured by light obscuration or membrane microscopy according to Ph. Eur. 2.9.19. Bacterial endotoxin limits are derived from the maximum single dose and the route of administration using Ph. Eur. 2.6.14; the upstream API acceptance value is set so that the final product does not exceed the compendial limit. Bulk solutions at 500 mg/mL require osmolarity adjustment by dilution into 0.9% sodium chloride or 5% glucose before infusion; compatibility studies should confirm the absence of precipitation and degradation products over the intended holding time.

    Stress testing under ICH Q1A identifies the main solution degradation route as hydrolytic, producing 4-methylaminoantipyrine and related substances; the manufacturing process therefore excludes copper and iron contact surfaces and uses nitrogen blanketing where possible. pH of the diluted product is measured by Ph. Eur. 2.2.3. Because the sodium salt dissociates rapidly, adding acidic drug solutions to the same infusion line can produce a pH shift and local precipitation; simultaneous administration with acidic injectables is evaluated by pH titration and visible-particle inspection before clinical use. The diluted solution should also be checked for sub-visible particles by Ph. Eur. 2.9.19 when the product is stored beyond the immediate-use period.

    Wet-granulation processing of this API is dominated by its high aqueous solubility. If an aqueous binder solution is used, a large fraction of the drug substance can dissolve and later reprecipitate during drying, producing hard granules with broad particle growth. The preferred fluid-bed granulation setup is a top-spray system with a hydroalcoholic binder or a binder solution of reduced water activity; the spray rate is adjusted so the bed remains granulating rather than forming a paste. Drying end-point is determined by loss on drying according to Ph. Eur. 2.2.32 rather than by fixed drying time, because residual water shifts the monohydrate hydration envelope and can reduce flow. In high-shear mixer trials, torque-rheometry measurements from production-scale mixers identify the wet-mass endpoint before the mass over-wets and blocks the discharge port. The dried granule is milled through a conical mill screen of 0.8 mm or 1.0 mm and then compressed or encapsulated. Granule size distribution is measured by sieving or laser diffraction; content uniformity of the final blend is verified by Ph. Eur. 2.9.6. Published data for twin-screw continuous granulation of this specific API is limited.

    Related substances are controlled by liquid chromatography according to Ph. Eur. 2.2.29, with the current monograph defining specified and unspecified impurities. The major degradation species in aqueous solution is 4-methylaminoantipyrine. Stability studies under ICH Q1A, ICH Q1B, and ICH Q1E are required to differentiate synthetic impurities from degradation products. The analytical worksheet records relative retention time, resolution between critical peak pairs, and signal-to-noise ratio at the reporting threshold. If the API is used in combination with excipients that alter pH or contain reducing functional groups, compatibility is tested by stress storage under ICH Q1A conditions; published data for this specific API-excipient configuration is limited.

    Differences from Paracetamol and Ibuprofen in Aqueous Solubility and Granulation Behaviour

    Compared with other non-opioid analgesic APIs, metamizole sodium occupies a different processing space. Paracetamol has aqueous solubility of approximately 14 mg/mL at 25 °C, and ibuprofen acid is practically insoluble in water under Ph. Eur. 5.11; metamizole sodium is freely soluble under the same classification. For injectable products, the concentration differential is operationally significant: metamizole sodium solutions at 500 mg/mL are established, whereas paracetamol infusions commonly use 10 mg/mL and ibuprofen parenterals require a salt or amino-acid complex. This high solubility also moves the critical granulation risk from poor wetting to dissolution-induced caking. Solid oral grades of metamizole sodium are not automatically suitable for parenteral use solely because they are chemically pure; endotoxin, bioburden, and sub-visible particle controls must be separately demonstrated.

    Comparative formulation-relevant properties of selected analgesic APIs
    PropertyAnalgin / metamizole sodium monohydrateParacetamolIbuprofen acid
    Aqueous solubilityFreely soluble; Ph. Eur. 5.11Approximately 14 mg/mL at 25 °CPractically insoluble; Ph. Eur. 5.11
    Typical high-concentration injectable strength500 mg/mL solution10 mg/mL infusionRequires salt or amino-acid complex
    Wet-granulation criticalityDissolution-induced caking when overwettedRemaining crystalline phase moderates wet massHydrophobic wetting and binder interaction require surfactant
    Primary aqueous instabilityHydrolysis to 4-methylaminoantipyrine and oxidative colourHydrolysis to 4-aminophenol and oxidative degradationAqueous degradation of the acid form is less immediate; stability is product-specific
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