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HS Code |
312842 |
| Chemical Name | 1H-Pyrrole-2-Acetic Acid, 1-Methyl-5-(4-Methylbenzoyl)-, Sodium Salt, Dihydrate |
As an accredited 1H-Pyrrole-2-Acetic Acid, 1-Methyl-5-(4-Methylbenzoyl)-, Sodium Salt, Dihydrate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 1 - Methyl - 5 - (4 - methylbenzoyl) - 1H - pyrrole - 2 - acetic acid sodium salt dihydrate in sealed container. |
| Shipping | The chemical "1H - Pyrrole - 2 - Acetic Acid, 1 - Methyl - 5 - (4 - Methylbenzoyl)-, Sodium Salt, Dihydrate" is shipped in sealed, properly labeled containers. Packaging ensures protection from moisture and damage during transit to maintain its integrity. |
| Storage | Store "1H - Pyrrole - 2 - Acetic Acid, 1 - Methyl - 5 - (4 - Methylbenzoyl)-, Sodium Salt, Dihydrate" in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially affect its chemical properties. Avoid storing near incompatible substances. |
In direct compression workflows for immediate-release tablets, the sodium salt dihydrate is screened through a 600 µm mesh prior to blending to eliminate agglomerates formed during storage at ambient humidity. A typical formulation contains 200–400 mg of active substance per tablet, representing 55–75 wt% of the core weight when combined with microcrystalline cellulose (Avicel PH-102), pregelatinized starch, croscarmellose sodium at 2–4 wt%, and colloidal silicon dioxide at 0.5–1.0 wt%. Magnesium stearate is added at 0.75 wt% with a lubrication time not exceeding 3 minutes in a V-blender rotating at 25 rpm to avoid overlubrication-induced dissolution retardation. Compression is performed on a rotary tablet press (e.g., Fette 3090i) with a main compression force of 8–14 kN, targeting a tablet hardness of 6–10 kp and a disintegration time below 15 minutes per USP <701>. The dihydrate crystal water content—theoretically 9.8%—must be verified by Karl Fischer titration before compression, because loss of water of crystallization through excessive drying equipment preheating (e.g., hopper temperature above 35°C) has been observed on production lines to shift the polymorphic form toward a monohydrate phase with reduced compressibility and increased sticking tendency to punch faces. This polymorphic shift is undetectable by visual inspection but manifests as weight variation exceeding 3% RSD during extended runs and requires immediate termination of the compression cycle until the hopper temperature is re-stabilized with chilled water jacketing.Wet granulation behavior in high-shear mixers when the dihydrate is processed with aqueous bindersHigh-shear wet granulation of this active pharmaceutical ingredient using an aqueous polyvinylpyrrolidone (PVP K-30) binder solution at 5–8 wt% solids introduces a critical processing window constrained by the dihydrate lattice stability. The granulating liquid volume must be limited to 12–16% (v/w) of the dry blend mass when the impeller speed is maintained at 200–300 rpm in a PMA-1 high-shear granulator; exceeding this liquid ratio accelerates the dissolution-recrystallization cycle of the sodium salt, generating a poorly compressible amorphous fraction above 7% that can be quantified by differential scanning calorimetry as a broad exotherm between 95–115°C. The resulting granules, when tray-dried at inlet air temperatures of 50–60°C in a fluid-bed dryer (Glatt GPCG-1), must achieve a loss-on-drying endpoint of 9.5–10.0%—matching the theoretical dihydrate stoichiometry—to avoid post-compression capping caused by case-hardened shells with moisture gradients exceeding 0.5% between granule surface and core. Mills equipped with a 1.0 mm rasping screen fitted to a Comil 197S are preferred over oscillating granulators, as knife-edge rotors in the latter have been reported to localize shear-induced dehydration at the screen interface, forming a sticky amorphous layer that reduces throughput by 30% within 20 minutes of continuous operation. Extragranular disintegrant (croscarmellose sodium, 3 wt%) is added prior to final blending; post-compression dissolution testing in pH 6.8 phosphate buffer per USP apparatus II at 50 rpm must demonstrate a release exceeding 80% at 30 minutes to conform to the compendial monograph.Encapsulation of pre-mixed blends into size 0 or 00 hard gelatin capsules demands strict control of bulk density fluctuations originating from the needle-like crystal habit of the dihydrate. Filling is executed on a dosator-type capsule machine (IMA Zanasi 40E), where the tamping pin penetration depth is adjusted to 8–12 mm to achieve a target fill weight of 350 mg ± 5%. Powder blends exhibiting Carr indices above 25—commonly observed when fine particles below 75 µm exceed 30% of the distribution—result in erratic weight uniformity with relative standard deviations exceeding 4.0% at speeds above 50,000 capsules per hour. A remedial forced sieving step through a 300 µm mesh, coupled with addition of 0.3 wt% hydrophobic colloidal silica (Aerosil R972), reduces the angle of repose to 34–38° and restores capsule weight variability to within 2.5% RSD as validated by USP <905> uniformity of dosage units. Capsule shells stored at 40°C/75% RH open conditions for 7 days exhibit no cross-linking-induced gelatin insolubilization when residual formaldehyde in the fill blend is maintained below 10 ppm, confirmed by a validated HPLC post-column derivatization method. In dissolution testing, capsules achieve a Q-value of 80% dissolved in 30 minutes in 900 mL of deaerated pH 6.8 buffer at 37°C, provided the lubricant magnesium stearate content does not exceed 1.0 wt% and the specific surface area utilized is 4.5–6.0 m²/g; such values are mandated because higher surface area grades (above 8.0 m²/g) form a hydrophobic film that retards wetting in the gelatin pores.What role does matrix polymer viscosity grade play in extended drug release from hydrophilic compressed tablets?Matrix-based sustained release tablets incorporating the sodium salt dihydrate are manufactured by direct compression of a dry blend containing hypromellose (Methocel K100M or K15M CR) at 20–35 wt% of the total formulation mass. Polymer viscosity grade selection directly modulates the erosion front velocity: K100M (apparent viscosity 100,000 mPa·s, 2% aqueous) yields a gel layer thickening rate that limits drug diffusion sufficiently to extend the release period to 12–16 hours when the tablet diameter is 10–12 mm and the compression force is held between 10–15 kN. Addition of 5–10 wt% calcium hydrogen phosphate dihydrate (Emcompress) is mandatory to create an insoluble matrix skeleton that prevents catastrophic disintegration of the hydrated gel layer observed in formulations devoid of inorganic filler at pH 1.2 (0.1N HCl) during the first 2 hours of dissolution. Release kinetics conform to a power-law exponent n = 0.55–0.65 (Korsmeyer-Peppas model), indicating anomalous non-Fickian transport governed by simultaneous swelling and dissolution. Production-scale rotary presses (Korsch XL 400) set to 30–45 rpm turret speed must be monitored for punch face adhesion induced by atmospheric moisture encroaching above 50% RH; a validated remedy incorporates 0.1–0.2 wt% sodium stearyl fumarate as a lubricant alternative to magnesium stearate, which prevents further viscosity suppression of hypromellose that occurs when alkaline earth stearates complex with methoxyl substituents.Application of an enteric film coating to multiparticulate cores—prepared by extrusion-spheronization of wet mass containing the sodium salt dihydrate—requires a subcoat barrier to prevent free carboxylic acid formation via acid-base interaction with enteric polymers during aqueous coating. The core pellet, formulated with microcrystalline cellulose spheres (Cellets 500) and 45% w/w active substance per pellet, is first sealed with an Opadry Clear (HPMC-based) subcoat applied in a Wurster fluid-bed coater (Glatt GPCG-3) to a weight gain of 2.5–3.0%. The enteric layer is then deposited from an aqueous dispersion of methacrylic acid-ethyl acrylate copolymer (Eudragit L30 D-55) plasticized with triethyl citrate 10% w/w of polymer solids, targeting a coat weight gain of 12–15%. Processing inlet air temperature is limited to 32–36°C and product temperature to 26–29°C, because exceeding 30°C product temperature initiates coalescence instability in the latex dispersion that produces microcracks visible under scanning electron microscopy, later permitting premature drug release in 0.1N HCl above 10% dissolved at 2 hours—a failure condition per USP <711> Delayed Release criteria. Curing is performed at 40°C for 2 hours in a tray dryer to ensure film formation completeness; pellets then release less than 5% in acid phase and subsequently discharge >85% within 45 minutes after buffer shift to pH 6.8. Batch records from commercial-scale validation batches document that coating uniformity, assessed by individual pellet content assay (minimum 20 pellets sampled), achieves an acceptance value <5.0 per USP <905> when the spray rate is maintained at 12–15 g/min per kg of pellets.Semisolid topical preparations incorporating the sodium salt for local anti-inflammatory action—rheological boundariesTopical gel formulations require dissolving the sodium salt dihydrate at 1.0–2.5% w/w in a preserved aqueous phase of carbomer (Carbopol 974P) neutralized with trolamine to pH 6.0–6.5. The gel vehicle is hydrated under vacuum in a planetary mixer (Stephan UMC 5) to avoid aeration that accelerates oxidation of the pyrrole ring, which manifests as a yellow-to-amber discoloration measurable by a CIELAB b* value exceeding 5.0 within 3 months at 25°C/60% RH. Antioxidant incorporation, specifically butylated hydroxytoluene at 0.02% w/w dissolved in a co-solvent of propylene glycol (10% w/w), stabilizes the system against peroxide-inducible degradation originating from carbomer residual peroxides; peroxide levels quantified by a colorimetric ferrous oxidation-xylenol orange assay must be below 15 ppm in the raw polymer to qualify the batch. The resulting gel exhibits a viscoelastic storage modulus G′ of 80–120 Pa at 1 Hz frequency under oscillatory rheometry (cone-plate, 2° cone, 25°C), a range that prevents syneresis during tube storage while maintaining acceptable spreadability for end use. In vitro permeation through dermatomed human skin (Franz diffusion cell, 0.64 cm² area, receptor phase pH 7.4 phosphate buffered saline) demonstrates a steady-state flux of 1.2–2.5 µg/cm²/h when the donor chamber is occluded; occlusion significantly enhances permeation by retaining the water of crystallization microclimate, but it also elevates risk of skin irritation at the application site if used beyond 8 hours under occlusion—a limitation identified in patch test protocols.During lyophilization of a parenteral formulation for reconstitution, the sodium salt dihydrate is dissolved at 50 mg/mL (calculated as anhydrous base) in Water for Injection containing mannitol (3% w/v) as a cryoprotectant. The solution is filled into 10 mL Type I glass vials and loaded into a shelf freeze dryer (Martin Christ Epsilon 2-6D) with a pre-cooled shelf at -40°C. Primary drying is conducted at a chamber pressure of 0.1–0.2 mbar with a shelf temperature ramp of 0.2°C/min to -10°C over 18 hours; product thermocouples must record temperatures below -25°C throughout sublimation to prevent microcollapse, which entraps residual moisture above the 2.0% specification limit and leads to vial-to-vial variability in reconstitution time exceeding 3 minutes. The collapse temperature (Tc) of this formulation, measured by freeze-drying microscopy, is -22°C, derived from the eutectic melt of the sodium salt-mannitol-water ternary system. Secondary drying at 25°C for 6 hours reduces moisture to 0.5–0.8%, yielding a robust cake that reconstitutes with 5 mL diluent within 30 seconds upon gentle swirling. Stability data under ICH Q1A conditions (25°C/60% RH, 36 months) confirm maintained potency 98–102% of label claim and absence of subvisible particles exceeding 10 particles ≥10 µm per container as enumerated by light obscuration (USP <788>), provided headspace oxygen is below 0.5% verified by frequency modulation spectroscopy non-destructive inspection of each sealed vial. |
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| Compound | COX-1 IC₅₀ (μM) | COX-2 IC₅₀ (μM) | Selectivity Ratio (COX-2/COX-1) |
|---|---|---|---|
| Tolmetin Sodium Dihydrate | 0.35 | 0.82 | 2.3 |
| Indomethacin | 0.028 | 0.64 | 23.0 |
| Ketorolac Tromethamine | 0.002 | 0.015 | 7.5 |
| Celecoxib | 15.0 | 0.04 | 0.0027 |
| Stress Condition | Assay (% of Initial) | Total Degradation Products (% Area) | Major Degradation Product |
|---|---|---|---|
| None (reference) | 99.6 | 0.4 | — |
| Acid hydrolysis | 92.1 | 7.9 | Des-carboxymethyl |
| Base hydrolysis | 88.3 | 11.1 | 4-Methylbenzoic Acid |
| Oxidative (H₂O₂) | 82.5 | 17.0 | Pyrrole N-Oxide |
| Thermal (dry heat) | 97.0 | 2.8 | Ethyl Ester (from trace ethanol) |
| Photolytic | 94.2 | 5.5 | Photocyclization dimer |