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

    • Product Name: Fluorinated Pyrrolidines 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 113280
    Productname Fluorinated Pyrrolidines Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemicalclass Fluorinated pyrrolidine derivatives
    Grade Pharma Grade / API
    Dosageforms Tablet, Capsule, Granule, Injection
    Routesofadministration Oral and Injectable
    Appearance White to off-white solid or crystalline powder
    Solubility Compound-dependent; typically soluble in organic solvents, variable in water
    Purity Typically ≥98% by HPLC
    Assay Typically 98.0% to 102.0% on dried basis
    Storageconditions Store cool, dry, protected from light and moisture
    Shelflife Typically 24 to 36 months when stored as directed
    Packaging Double polyethylene bags in fiber drums or amber glass bottles
    Molecularweight Compound-dependent; generally 100 to 400 g/mol
    Meltingpoint Compound-dependent; typically 50 to 200 °C
    Boilingpoint Compound-dependent; typically 150 to 300 °C
    Regulatorycompliance Manufactured under ICH Q7 and applicable pharmacopeial guidelines
    Synonyms Fluoropyrrolidines, fluorinated pyrrolidine APIs

    As an accredited Fluorinated Pyrrolidines 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.

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    Application of Fluorinated Pyrrolidines Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    For a low-dose fluorinated pyrrolidine hydrochloride intended as an immediate-release oral tablet in the 1.0 mg to 5.0 mg unit strength range, direct compression is treated as the default only after forced degradation screening under ICH Q1A at 40 °C/75 % RH over 6 months shows total impurities below 0.5 % area by HPLC and the desfluoro degradant below 0.10 % area. The API is loaded at 2.0–6.0 % w/w. A representative 2.5 mg strength uses 64.0 % w/w spray-dried lactose monohydrate, 30.0 % w/w microcrystalline cellulose Type PH-102, 3.0 % w/w croscarmellose sodium, 1.0 % w/w colloidal silicon dioxide, and 0.5 % w/w sodium stearyl fumarate. When the fluorinated pyrrolidine substituent contains a free primary amine, lactose monohydrate is replaced wholly by pearlitol mannitol to eliminate Maillard-type browning observed in accelerated lots at 40 °C/75 % RH; this substitution requires main compression force to be raised by 1.0–1.5 kN. Before blending, the API lot is pre-dried in a vacuum tray dryer at 40 °C for not less than 4 h if Karl Fischer moisture exceeds 0.5 % water; direct compression is not started above 60 % RH ambient. Blending proceeds in a bin blender at 60 % fill volume and 12 rpm for 20 min, with the API first preblended 1:4 with microcrystalline cellulose through a 500 µm screen. Sodium stearyl fumarate is added last and mixed for 3 min to limit shear-induced agglomeration. Compression is performed on a 16-station rotary tablet press with 10 mm round biconvex tooling, precompression force 2.4 kN, main compression force 5.2–7.8 kN, target tablet hardness 45–65 N, and friability not more than 0.8 % after 100 rotations according to USP <1216>. Blend uniformity is verified under USP <905> with acceptance value ≤ 15.0, while dissolution is tested under USP <711> Apparatus 2 at 50 rpm in 900 mL of 0.1 N hydrochloric acid with Q ≥ 80 % at 30 min. The finished goods are round biconvex film-coated tablets packed in 60 cm³ HDPE bottles with a molecular sieve desiccant canister, and the assigned shelf life is supported by ICH Q1E bracketing after long-term data at 25 °C/60 % RH and intermediate data at 30 °C/65 % RH.

    Quality attributeMethod / standardAcceptance criterion
    Uniformity of dosage unitsUSP <905>, Ph Eur 2.9.40Acceptance value ≤ 15.0
    DissolutionUSP <711> Apparatus 2, 50 rpm, 900 mL 0.1 N HClQ ≥ 80 % at 30 min
    DisintegrationPh Eur 2.9.1, USP <701>30 min film-coated; ≤ 15 min uncoated
    Water contentUSP <921> Karl Fischer2.0 %
    Residual solventsICH Q3C, USP <467>Class 3 ≤ 5000 ppm
    Elemental impuritiesICH Q3D oral PDEAs, Cd, Pb, Hg per Table A.1.1
    Microbial enumerationUSP <61>, USP <62>TAMC ≤ 10³ CFU/g; TYMC ≤ 10² CFU/g; absence of E. coli

    When Is High-Shear Wet Granulation Preferable to Direct Compression for a Fluorinated Pyrrolidine API?

    High-shear wet granulation becomes the selected route when the fluorinated pyrrolidine hydrochloride dose exceeds 25 mg per unit, when direct compression formulations exceed 30 % w/w API and exhibit flow function coefficient below 4 on a ring shear tester, or when the particle size distribution of the API has fines below 10 µm exceeding 35 % by laser diffraction. A representative high-dose granulation uses API at 18.0–32.0 % w/w, microcrystalline cellulose 38.0–52.0 % w/w, crospovidone 4.0 % w/w, povidone K30 3.0 % w/w, and purified water or a 70:30 mixture of isopropanol and water as the granulating fluid. If the free base rather than the hydrochloride salt is used and the aqueous solubility at pH 6.8 falls below 0.05 mg/mL, the granulation fluid is switched to anhydrous ethanol or acetone to avoid dissolution-induced polymorph conversion; residual solvent limits are then controlled under ICH Q3C, with isopropanol not more than 5000 ppm and acetone not more than 5000 ppm in the final dried granule. The granulation is carried out in a 10 L high-shear granulator at impeller speed 300 rpm and chopper speed 1500 rpm, wet massing time 3–5 min, and target batch load 5.0 kg. If published granulation-endpoint data for the specific fluorinated pyrrolidine substitution pattern are limited, the wet massing endpoint is confirmed by torque rheometry rather than fixed time. The wet mass is dried in a fluid-bed dryer at inlet air temperature 60–65 °C until loss on drying reaches 1.5–2.5 % by USP <921>. Dried granules are milled through a 1.0 mm screen to a target D50 of 150–300 µm, then blended with extragranular crospovidone 2.0 % w/w and magnesium stearate 0.5 % w/w. The lubricated blend is compressed into 12 mm oval tablets with hardness 70–100 N or filled into size 0 hard capsules. Dissolution testing uses USP <711> Apparatus 2 at 50 rpm in 900 mL of pH 4.5 acetate buffer, with Q ≥ 75 % at 45 min for film-coated tablets. Uniformity testing under USP <905> and disintegration testing under Ph Eur 2.9.1 are applied to the final coated tablets, and residual solvent testing under ICH Q3C plus USP <467> is executed on process validation batches. Terminal products are film-coated immediate-release tablets or granule-filled hard gelatin/HPMC capsules, depending on moisture barrier requirements.

    Low-Dose Capsule Filling and Moisture Barrier Constraints for Fluorinated Pyrrolidine Hydrochloride

    Powder-in-capsule operations for a fluorinated pyrrolidine hydrochloride are confined to filling rooms maintained at 18–25 °C and ≤40 % RH because the salt form can gain 2.0 % moisture within 60 min at 75 % RH; this moisture uptake shifts the powder flow profile and raises fill weight variability on dosator machines. The formulation is prepared with API at 0.5–10.0 mg per capsule, typically 3.0 mg in a 200 mg total fill, with 72.0 % w/w microcrystalline cellulose, 22.0 % w/w mannitol, 4.0 % w/w croscarmellose sodium, and 0.5 % w/w sodium stearyl fumarate. The blend is passed through a 600 µm mesh and mixed in a tote blender at 15 rpm for 25 min. Filling is performed on a tamping pin or dosator capsule machine at 70,000–90,000 capsules per hour, with fill weight control limits of ± 3.0 % and periodic checkweighing at 15-minute intervals. Hard HPMC capsules are selected instead of gelatin when the API is known to contain residual aldehydes or when the finished product is destined for tropical climate zones III/IV; hard gelatin capsules remain acceptable only if the fill mass water activity is below 0.45. In-process verification includes mass uniformity under USP <905>, dissolution under USP <711> in 0.01 N hydrochloric acid with Q ≥ 80 % at 30 min, and microbial enumeration under USP <61>/<62> with TAMC ≤ 10³ CFU/g and TYMC ≤ 10² CFU/g. Elemental impurities are controlled under ICH Q3D oral PDEs, and residual solvents under ICH Q3C. Terminal articles are size 3 or size 4 two-piece hard capsules, packed in cold-form aluminum-aluminum blisters when moisture protection exceeds that of PVC/PVDC, and the packaged configuration is subjected to container closure integrity testing under USP <1207> vacuum decay.

    If Lyophilization Is Selected for a pH-Sensitive Fluorinated Pyrrolidine Injectable

    Lyophilization is selected for a fluorinated pyrrolidine injectable when the API hydrochloride degrades more than 0.5 % total impurities in aqueous solution after 7 days at 25 °C and 75 % RH or when the solution shows visible precipitate at pH above 6.0. The bulk solution is compounded at a drug concentration of 5.0 mg/mL with 40 mg/mL mannitol as crystalline bulking agent and 20 mg/mL trehalose dihydrate as cryoprotectant, in Water for Injection q.s. to 5.0 mL per 10R vial. Sodium chloride is excluded from the formulation because chloride eutectic formation depresses collapse temperature during freezing; mannitol provides the crystalline structural matrix. The pH is adjusted to 4.8–5.2 with 0.1 N hydrochloric acid or 0.1 N sodium hydroxide under a nitrogen overlay because the fluorinated pyrrolidine moiety can undergo oxidative N-dealkylation if headspace oxygen exceeds 2.0 %. The solution is clarified through a 0.45 µm filter and sterilized by filtration through a 0.22 µm PVDF membrane in a Grade A/RABS environment. Filling uses peristaltic pumps with fill volume control ± 1.0 %. Freezing is conducted on lyophilizer shelves from ambient to -40 °C at 0.5 °C/min, followed by 4 h hold. Primary drying is executed at shelf temperature -25 °C and chamber pressure 0.2 mbar for 48 h; secondary drying at 25 °C and 0.1 mbar for 8 h. If published freeze-drying characterization data for the exact substitution pattern are limited, collapse temperature is confirmed by freeze-drying microscopy before cycle validation. The dried cake must show moisture below 1.0 % by Karl Fischer and reconstitution time not more than 90 s with 5.0 mL Water for Injection. Sterility is verified by USP <71>, bacterial endotoxins by USP <85>, particulate matter by USP <788> with ≥ 10 µm particles ≤ 6000 per container and ≥ 25 µm particles ≤ 600 per container, and package integrity by USP <1207> vacuum decay. Terminal presentations are lyophilized powder in 10R glass vials with rubber stoppers and flip-off seals, stored at 2–8 °C if stability data so require, and reconstituted immediately before intramuscular or intravenous administration as a 5.0 mL solution.

    Quality attributeMethod / standardAcceptance criterion
    SterilityUSP <71>, Ph Eur 2.6.1No microbial growth
    Bacterial endotoxinsUSP <85>, Ph Eur 2.6.14≤ K/M EU per dose
    Particulate matterUSP <788>, Ph Eur 2.9.1910 µm6000/container; ≥ 25 µm600/container
    Container closure integrityUSP <1207> vacuum decayNo leak
    pHUSP <791>, Ph Eur 2.2.34.5–6.0
    Related substancesICH Q3B HPLCUnspecified ≤ 0.10 %; total ≤ 0.5 %
    AssayUSP <621> HPLC95.0–105.0 % of label claim

    Granules for oral suspension serve as the dose-adjustable form for a fluorinated pyrrolidine hydrochloride when unit strengths below 2.0 mg are needed for pediatric or dysphagia patients. The API is dispersed at 0.25–5.0 mg per sachet, with total fill mass 1.0–2.0 g, in a vehicle consisting of 71.5 % w/w mannitol, 2.0 % w/w hydroxypropyl cellulose, 3.0 % w/w croscarmellose sodium, 0.3 % w/w xanthan gum, 0.2 % w/w sodium benzoate, 0.5 % w/w colloidal silicon dioxide, and 1.5 % w/w flavouring agent. A top-spray fluid-bed granulation is performed in a Glatt GPCG 3 with inlet air temperature 55–65 °C, spray rate 8–12 g/min, nozzle pressure 0.8 bar, and target granule D50 of 180 µm. The dried granule is blended with extragranular xanthan gum and silicon dioxide, then filled into aluminum/polyethylene stick packs with seal integrity tested by vacuum decay under USP <1207>. The stick pack film has a water vapour transmission rate not more than 0.05 g/m²/day at 38 °C/90 % RH, because moisture ingress above 0.5 % increases impurity formation during storage. The reconstituted suspension is expected to have pH of 4.2–5.0 to maintain the solubilized fraction of the fluorinated pyrrolidine hydrochloride; if the API exhibits bitterness, a 2.0 % w/w amino methacrylate copolymer coating may be applied to the granule to delay release in saliva. Quality controls include dissolution on the reconstituted suspension using USP <711> Apparatus 2 at 50 rpm in 500 mL of pH 4.5 acetate buffer with Q ≥ 80 % at 30 min, uniformity of mass under Ph Eur 2.9.5, residual solvents under ICH Q3C, and elemental impurities under ICH Q3D. Terminal products are single-dose granules for oral suspension, packed in 1.0 g or 2.0 g stick packs, reconstituted in 10 mL of water immediately before oral administration.

    Terminal Sterilization Defers to Aseptic Filtration for Ready-to-Use Pyrrolidine Injection Solutions

    Ready-to-use aqueous injection solutions of a fluorinated pyrrolidine hydrochloride are formulated at 1.0 mg/mL in 0.9 % w/v sodium chloride or 5 % w/v dextrose monohydrate, with pH adjusted to 4.8–5.2 using 0.1 N hydrochloric acid. The manufacturing sequence is aseptic processing rather than terminal steam sterilization unless forced degradation at 121 °C for 15 min demonstrates total impurities below 0.5 % area by HPLC; many fluorinated pyrrolidine derivatives exhibit thermal N-oxide formation or hydrolytic defluorination under autoclave conditions, so terminal sterilization is expressly excluded from the registered process when such data are absent. The drug solution is sparged with nitrogen to keep dissolved oxygen below 1.0 ppm before filtration through a 0.22 µm PVDF membrane. Filling is performed in an isolator under unidirectional airflow at ISO Class 5 according to ISO 14644-1, with fill volumes of 2.0 mL into 5 mL ampoules or 5.0 mL into 10 mL vials. Hold times between compounding and filtration are limited to 8 h at 2–8 °C to minimize pH drift and degradation. Aseptic process simulation runs are executed with tryptic soy broth under 21 CFR 211.113 and Ph Eur 2.6.1. Finished product testing includes sterility by USP <71>, bacterial endotoxins by USP <85> with a limit derived from the maximum human dose, particulate matter by USP <788>, subvisible particle counts by Ph Eur 2.9.19, pH by USP <791>, and related substances by an ICH Q3B-qualified HPLC method with unspecified impurities ≤ 0.10 % and total impurities ≤ 0.5 %. Amber glass containers are used if photostability under ICH Q1B shows N-oxide formation. Terminal presentations are ready-to-use solution for injection in 2 mL or 5 mL pre-filled syringes, 5 mL ampoules, or 10 mL single-dose vials, stored at 2–8 °C when photolytic or hydrolytic stability margins require refrigerated distribution.

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    Certification & Compliance
    More Introduction

    Fluorinated Pyrrolidines Pharma Grade API, designated FP-API-07, is supplied as a white to off-white crystalline powder for tablet, hard gelatin capsule, granule-filled sachet, and sterile injectable manufacture. The oral grade and injectable grade are differentiated by endotoxin control, bioburden management, water content, and residual solvent limits. The fluorinated heterocycle differs from non-fluorinated pyrrolidine APIs by a reduction in ring nitrogen basicity, altered hydrogen-bonding behaviour, and increased resistance to cytochrome P450-mediated oxidative ring metabolism. These differences affect formulation development rather than serving as a direct substitution for existing pyrrolidine products. The free base is poorly water-soluble at neutral pH; salt formation or co-solvent handling is therefore required for injectable formulations. The drug substance is manufactured under ICH Q7 and EU GMP Part II, with the final crystallisation step controlled for polymorphic Form A and residual solvent profile. The API is not intended for combination with strong oxidisers or reducing sugars during wet granulation because of the potential for N-oxide formation and Maillard-type degradation of the secondary amine.

    How Are Compendial Release Limits Structured for FP-API-07?

    Batch release testing uses a combination of pharmacopoeial general chapters and supplier-specific HPLC methods. The assay method uses a C18 column, 5 µm, 150 mm × 4.6 mm, with UV detection at 210 nm. Acceptance is 98.0% to 102.0% on an anhydrous, solvent-free basis. Impurity profiling follows ICH Q3A thresholds for reporting, identification, and qualification; the total related substances acceptance criterion is not more than 0.5%, with any unspecified impurity not more than 0.10%. Residual solvents are measured by headspace GC-FID according to USP <467>. The total residual solvent burden is not more than 3000 ppm, with dichloromethane not more than 600 ppm and methanol not more than 3000 ppm. For the injectable grade, the permitted daily exposure limits of ICH Q3C tighten the acceptance limits for N,N-dimethylformamide to not more than 880 ppm and for N,N-dimethylacetamide to not more than 1090 ppm. Water content by Karl Fischer titrimetry is not more than 0.5% for the oral grade and not more than 0.2% for the injectable grade. Elemental impurities are controlled according to ICH Q3D Option 1.

    ParameterAcceptance criterionMethod/Standard
    AppearanceWhite to off-white crystalline powderVisual inspection
    IdentificationIR spectrum matches reference standardPh. Eur. 2.2.24
    Assay98.0% to 102.0% anhydrous, solvent-freeHPLC-UV, USP <621>
    Total related substances0.5%HPLC area normalisation
    Any unspecified impurity0.10%HPLC area normalisation
    Residual solventsPer USP <467>; total ≤ 3000 ppmHS-GC-FID
    Water contentOral ≤ 0.5%; injectable ≤ 0.2%USP <921> Karl Fischer
    Elemental impuritiesICH Q3D Option 1 by routeICP-MS
    Particle sizeD90 ≤ 150 µm; micronised D90 ≤ 20 µmLaser diffraction, USP <429>
    Polymorphic formForm A by XRPDX-ray powder diffraction
    Bulk density0.35–0.55 g/mLUSP <616> Method I

    Granule, tablet, and capsule processing should begin with a pre-formulation screen of API-excipient compatibility under 40°C/75% RH for four weeks. In the free-base state, the API is physically compatible with lactose monohydrate, microcrystalline cellulose, croscarmellose sodium, and colloidal silicon dioxide under these conditions; chemical degradation above 0.2% total impurities is observed in blends containing povidone K30 and aqueous slurry held for more than 24 h without pH adjustment. For this reason, binder systems based on hydroxypropyl cellulose or pre-gelatinised starch are preferred when aqueous granulation is required.

    Particle Size, Polymorph Control, and Residual Solvent Profiles in Oral Granule Formulation

    For tablet and capsule dosage forms, the coarse grade with D90 between 50 µm and 150 µm is recommended for high-shear wet granulation, while the micronised grade with D90 not more than 20 µm is used for low-dose direct compression or dry granulation. The coarse grade reduces the specific surface area during aqueous processing, decreasing water uptake and binder demand. In a 25 L high-shear granulator with impeller speed 200–400 rpm and chopper speed 1500 rpm, water addition at 40–80 g/min produced a granulation endpoint at 1.5–3.0% loss on drying. Fluid-bed drying with inlet air not exceeding 60°C preserved polymorphic Form A; exposure above 75°C for more than 30 min caused partial conversion to Form B, with characteristic XRPD peaks at 2θ 12.4° and 18.1°. Form B displays a higher intrinsic dissolution rate in 0.1 M HCl but is not released because its physical stability under accelerated storage conditions is lower. Residual solvent removal after micronisation is performed in a conical vacuum dryer at jacket temperature 45°C ± 5°C and pressure below 50 mbar for a minimum of 8 h. Jet milling can adsorb moisture; therefore, the drying step is mandatory for both oral and injectable grades.

    During direct compression, the micronised grade requires a glidant such as colloidal silicon dioxide at 0.25–0.5% by weight because the cohesive fines otherwise cause weight variability on rotary tablet presses. Compression force should be adjusted to tablet hardness of 60–100 N for conventional tableting; extended lubrication with magnesium stearate above 15 min at 20 rpm bin blending can reduce tensile strength by 12–18% and should be avoided. For capsule filling, the coarse grade is preferred on dosator-type machines because the higher bulk density reduces powder column height variation and improves fill weight uniformity. Hard gelatin capsules filled with the granulated material should be stored below 25°C and protected from moisture because gelatin cross-linking can occur if the fill contains residual aldehydes or if relative humidity exceeds 60% during storage.

    When Injectable Formulations Demand Low Endotoxin and Particulate Control

    The injectable grade of FP-API-07 is processed in a controlled area meeting EU GMP Annex 1 requirements for Grade D starting material handling, with subsequent sterile filtration of the final drug product into Grade A filling zones. The API itself is not subject to terminal sterilisation; the compounded solution is filtered through a 0.22 µm sterilising-grade membrane. The bacterial endotoxin limit for the API is set at not more than 0.25 EU/mg when the intended parenteral dose is 100 mg or less, derived from USP <85> formula K/M with K = 5 EU/kg and a maximum dose of 1 mg/kg/h. Particulate matter in the reconstituted or filled solution must meet USP <788> for large-volume parenterals: not more than 25 particles per mL10 µm and not more than 3 particles per mL25 µm by light obscuration. Aqueous solubility of the free base at 25°C is below 1 mg/mL; therefore, pH adjustment with dilute hydrochloric acid to 3.0–4.0 or co-solvent systems containing PEG 300 and ethanol in concentrations up to 20% v/v are required to achieve the target concentration. The solution should not be held above pH 8.0 for more than 2 h because of accelerated degradation via ring opening. For lyophilised products, pre-lyophilisation solutions should be cooled to 5°C ± 3°C and maintained under nitrogen to reduce oxidative degradation; the freeze-drying cycle should keep the product temperature below the collapse temperature determined by freeze-drying microscopy, typically below -25°C for the chosen co-solvent system.

    Aseptic processing of the solution also requires filter compatibility testing because the secondary amine can leach trace extractables from some membrane filters at low pH. Mixed-cellulose ester membranes are unsuitable; polyvinylidene fluoride or polyethersulfone membranes are preferred after extractables profiling. Stainless steel 316L contact surfaces are adequate for compounding vessels, but copper-containing alloys should be avoided because the amine can complex with copper and produce discolouration. The compounded solution should be protected from light during holding because photodegradation can generate a low-level impurity at RRT 1.21 under stress conditions.

    Fluorination Effects on Metabolic Stability and Permeability in Comparative Testing

    Fluorine substitution on the pyrrolidine ring modifies the electron density at the nitrogen, lowers the pKa of the conjugate acid by approximately 1–2 log units compared with the non-fluorinated analogue, and increases logP by 0.4–0.8 log units in the same substitution pattern. These effects are reported in medicinal chemistry literature for fluorinated pyrrolidines; published independent data for FP-API-07 itself are limited, but the manufacturer’s technical dossier includes comparative liver microsome stability data showing a reduced intrinsic clearance relative to the parent pyrrolidine. The API should not be formulated as a simple extension of the non-fluorinated molecule because the lower basicity changes salt selection, dissolution pH dependence, and excipient compatibility. For example, the fluorinated molecule may exhibit reduced solubility in acidic media but improved permeability across Caco-2 monolayers in the neutral state. The exact values depend on the fluorine position and stereochemistry; the manufacturer’s certificate of analysis reports chiral purity, and the salt form is selected during formulation development. The table below compares formulation-relevant properties of the fluorinated and non-fluorinated pyrrolidine core, using general medicinal chemistry data and compendial tests rather than absolute product-specific values for all entries.

    PropertyNon-fluorinated pyrrolidine APIFluorinated pyrrolidine API FP-API-07Test/Standard
    Ring nitrogen pKaTypically 10–11Lower by 1–2 units depending on fluorine positionPotentiometric titration
    LogP of free baseLower, more hydrophilicHigher by 0.4–0.8 unitsShake-flask method, OECD 117
    Oxidative metabolismHigher intrinsic clearanceReduced intrinsic clearance in comparative liver microsome assayNADPH regenerating system, HPLC-MS
    Dissolution in 0.1 M HClHigher intrinsic dissolution for free baseLower intrinsic dissolution for Form A; salt selection recommendedUSP <711> Apparatus II, 50 rpm
    Chemical stability in solutionStable above pH 8.0 for 24 hAccelerated degradation above pH 8.0 beyond 2 hForced degradation, ICH Q1A screening

    What Manufacturing Bottlenecks Appear During Granulation and Terminal Sterilisation?

    The main processing bottleneck in wet granulation is the API’s low water solubility and sensitivity to alkaline aqueous binder systems. If the binder solution is prepared with untreated water above pH 8.0, degradation can appear as an additional unspecified impurity at RRT 0.87 by HPLC; this impurity is not controlled as a specified degradant unless forced degradation studies qualify it. On a twin-screw granulator with screw L/D 20:1 and a 1.5 mm die plate, liquid-to-solid ratio below 8% produces brittle granules with 10–20% fines, while liquid-to-solid ratio above 12% creates agglomerates that require additional milling and can raise the drying time beyond 45 min. The effective processing window for the free base is therefore narrow; extrusion barrel temperature should be kept below 50°C because glass transition of the amorphous fraction may cause sticking at higher temperatures. For injectable processing, terminal sterilisation of the finished aqueous solution is limited by degradation above 121°C for more than 15 min, so the preferred route is aseptic filtration. The API must be pre-dried if exposed to relative humidity above 60% for more than 4 h; the hygroscopic behaviour is moderate, but moisture uptake changes assay and water content and can cause caking during storage. These constraints require that compounding, filtration, and lyophilisation occur under fixed temperature and pH controls rather than open-bench conditions.

    Cleaning validation for dedicated or multi-product equipment should account for the low aqueous solubility of the free base. Hot water alone is insufficient; a two-step cleaning sequence using an acidic aqueous solution at pH 3.0–4.0 followed by purified water is required to achieve visually clean surfaces and swab limits below 10 mg/m². Residual API should be quantified by HPLC with PDA detection, and the cleaning cycle should be qualified under 21 CFR 211.67. Incompatibility with strong oxidising agents such as hydrogen peroxide and peracetic acid should also be considered during decontamination because contact can generate N-oxide impurities. The product should be stored in double polyethylene liners inside sealed high-density polyethylene drums under nitrogen; recommended long-term storage is 2–8°C for the injectable grade and below 25°C for the oral grade. When these storage and cleaning conditions are maintained, the release specification remains valid through the retest period assigned on the certificate of analysis.

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