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2,3-DIAMINOPYRIDINE Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: 2,3-DIAMINOPYRIDINE Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 722331
    Product Name 2,3-DIAMINOPYRIDINE Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Api Name 2,3-Diaminopyridine
    Synonyms Pyridine-2,3-diamine; 2,3-Pyridinediamine; 2,3-Diaminopyridine
    Cas Number 40851-96-5
    Molecular Formula C5H7N3
    Molecular Weight 109.13 g/mol
    Grade Pharma Grade / API
    Assay Purity ≥99.0% by HPLC
    Appearance Off-white to light brown crystalline powder
    Solubility Soluble in water, methanol, ethanol; slightly soluble in nonpolar solvents
    Melting Point 82-86 °C
    Boiling Point 304.1 °C at 760 mmHg
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Storage Conditions Store in a cool, dry, well-ventilated place, protected from light and moisture
    Shelf Life 24-36 months in unopened original packaging
    Packaging 1 kg, 5 kg, 25 kg HDPE drums or as per customer requirement
    Quality Standard Manufactured under GMP conditions; HPLC assay ≥99.0%

    As an accredited 2,3-DIAMINOPYRIDINE 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 2,3-DIAMINOPYRIDINE Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    What Limits Blend Uniformity in Low-Dose Direct Compression Tablets?

    2,3-Diaminopyridine Pharma Grade API is incorporated into immediate-release tablet cores at 0.5–5.0% w/w for low-dose strengths and 5.0–25.0% w/w for standard strengths. Low-dose direct compression imposes a segregation constraint: the API is jet-milled to D90 ≤ 50 µm on a spiral fluid-jet mill with compressed air at 6 bar, and particle size is confirmed by laser diffraction per USP <429>. The milled API is pre-blended with microcrystalline cellulose Ph. Eur. 10.6 in a 1:9 ratio before addition of mannitol or dicalcium phosphate dihydrate. Reducing sugars such as lactose monohydrate require forced degradation screening under ICH Q1A(R2) because the two primary amine groups may form Maillard adducts; published data for this specific conjugation is limited, and a reducing-sugar-free formulation is preferred unless forced degradation data demonstrate absence of adducts. Blend uniformity is evaluated under USP <905>; relative standard deviation ≤ 5.0% is required for process validation batches, and final tablet content uniformity must meet USP <905> acceptance value ≤ 15.0. Dissolution testing follows USP <711> apparatus 2 at 50 rpm in 900 mL of 0.01 N hydrochloric acid with sinkers where required; Q = 80% at 30 min applies to immediate-release claims. Compression is performed on a Korsch XL 400 rotary tablet press with 49 Euro B stations at 30–60 rpm, using precompression force 2–4 kN and main compression force 8–15 kN to reach tablet hardness 60–100 N measured by USP <1217>. Tablets are film-coated with Opadry II aqueous dispersion to 2.0–3.0% w/w weight gain in a perforated pan coater at 50–60°C inlet air. The terminal finished product is immediate-release film-coated tablet. Compliance includes ICH Q3D(R2) elemental impurities, ICH Q3A API impurities, ICH Q1A(R2) stability, 21 CFR 211.110 in-process controls, EU GMP Part II for active substance handling, and ICH Q7 API GMP.

    For hard gelatin and HPMC capsule filling lines, 2,3-diaminopyridine Pharma Grade API is formulated at 2.0–50.0% w/w in size 0 to 3 capsules with fill weight targets between 80 mg and 250 mg. The dry blend is filled on an MG2 Planeta dosator or Bosch GKF 2600 tamping-pin machine at 30,000–60,000 capsules/h, with fill weight monitored every 30 min under 21 CFR 211.110 and acceptance limits of ± 5.0% of target. Disintegration is evaluated per USP <701> and dissolution by USP <711>; stability follows ICH Q1A(R2), elemental impurity control follows ICH Q3D(R2), and residual aldehydes from capsule shell raw material are controlled under ICH M7 because of primary amine reactivity. Terminal finished product is immediate-release hard capsule.

    Granulation Binder Selection and Moisture Control for Amine-Bearing Granules

    For oral granules packaged in single-dose sachets, the API is incorporated at 1.0–15.0% w/w of the dry granule mass, with a formulation composed of mannitol, microcrystalline cellulose, and low-substituted hydroxypropyl cellulose as disintegrant. High-shear wet granulation is performed in a Lödige LCF 100 L mixer at chopper speed 1,500 rpm and impeller speed 200–300 rpm; purified water or a 2.0–3.0% w/w povidone K30 binder solution is delivered at 0.5–1.5 kg/min until the mixer power consumption plateau indicates granule formation. The wet mass is discharged through a 4 mm coarse screen and dried in a Glatt GPCG 120 fluid-bed dryer with inlet air temperature 50–60°C; drying continues until residual moisture is ≤ 1.0% w/w by Karl Fischer titration USP <921>. Dried granules are milled through a 0.8 mm screen, and particle size distribution is determined by sieve analysis USP <786> with 90% of mass between 125 µm and 710 µm. Powder flowability is measured by USP <1174>; Carr index ≤ 20% is targeted for high-speed sachet filling. Terminal product is single-dose granules for oral suspension or direct administration. Compliance references include ICH Q3D(R2), ICH Q3A, 21 CFR 211.110, Ph. Eur. 2.9.36 for flow characterisation, and USP <905> for sachet content uniformity. Lactose is excluded as a binder because of primary-amine Maillard risk; mannitol is selected as the non-reducing diluent. Published data for 2,3-diaminopyridine granule stability under tropical humidity is limited; therefore, Alu/Alu sachet packaging with moisture vapour transmission rate ≤ 0.001 g/m²/day is used.

    Route-specific compliance and in-process control matrix for 2,3-diaminopyridine Pharma Grade API
    Dosage formControl pointStandard/methodTypical acceptance range
    Immediate-release tabletBlend uniformityUSP <905>RSD ≤ 5.0%
    Immediate-release tabletDissolutionUSP <711>Q = 80% at 30 min
    Hard capsuleFill weight21 CFR 211.110± 5.0% target
    Oral granuleResidual moistureUSP <921>≤ 1.0% w/w
    Injectable solutionParticulate matterUSP <788>≥10 µm: NMT 6,000 per container
    Injectable solutionEndotoxinUSP <85>≤ 0.25 EU/mg
    Lyophilized powderResidual moistureUSP <921>≤ 0.5% w/w
    All parenteralSterilityUSP <71>No growth

    Dissolved oxygen and headspace gas composition determine the injectable solution route for 2,3-diaminopyridine Pharma Grade API, because the pyridine ring and primary amine groups require oxidation control. In water-for-injection systems, the API is dissolved at 1.0–20.0 mg/mL, and pH is adjusted with hydrochloric acid or sodium hydroxide to 3.0–5.0; the exact pH is fixed by forced degradation studies under ICH Q1A(R2) and ICH Q3B. Nitrogen sparging reduces dissolved oxygen to ≤ 0.2 ppm before filtration. The solution is pre-filtered through 0.45 µm polyvinylidene fluoride and sterilized through two redundant 0.22 µm sterilizing-grade filters under EU GMP Annex 1 aseptic processing. Filling occurs in an ISO 14644-1:2015 Class 5 isolator or RABS with laminar airflow velocity 0.36–0.54 m/s; oxygen-sensitive headspace is overlaid with sterile nitrogen. Terminal sterilization by autoclaving at 121°C for 15 min is evaluated per Ph. Eur. 5.1.1; published data for 2,3-diaminopyridine aqueous degradation under this specific cycle is limited, and aseptic filtration is adopted when assay loss exceeds 0.5% or unknown impurities exceed 0.1% in the terminal cycle. Particulate matter is controlled per USP <788>: for containers ≤ 100 mL, particle counts ≥ 10 µm must not exceed 6,000 per container and ≥ 25 µm must not exceed 600 per container. Sterility is verified by membrane filtration per USP <71>; endotoxin is controlled per USP <85> with limit ≤ 0.25 EU/mg if the parenteral product is not intended for intrathecal use. Terminal finished product is aqueous solution for injection in 2 mL to 20 mL amber borosilicate vials or ampoules. Compliance includes 21 CFR 211, EU GMP Annex 1, ICH Q3D(R2), and ICH Q1A(R2).

    Formulation addition ratio and critical process window by dosage form
    Dosage formAPI addition ratioCritical process parameterControl range
    Immediate-release tablet0.5–25.0% w/wCompression force8–15 kN
    Hard capsule2.0–50.0% w/wLubricant level0.25–0.5% w/w
    Oral granule1.0–15.0% w/wResidual moisture≤ 1.0% w/w
    Injectable solution1.0–20.0 mg/mLDissolved oxygen≤ 0.2 ppm
    Lyophilized powder5.0–20.0% w/w total solidsPrimary drying shelf temperature-20°C ± 5°C

    When Lyophilization Replaces Terminal Sterilization in Injectable Processing

    For parenteral products requiring higher stability, 2,3-diaminopyridine Pharma Grade API is formulated as a lyophilized powder for reconstitution. The pre-lyophilization solution contains the API at 5.0–20.0% w/w of total solids, with mannitol as bulking agent at 2.0–5.0% w/w and sucrose or trehalose as cryoprotectant at 1.0–3.0% w/w. The solution is filtered through 0.22 µm sterilizing filters and filled into 5 mL or 10 mL borosilicate tubing vials with bromobutyl stoppers in a restricted-access barrier system. Lyophilization is performed in a Hull or BOC Edwards freeze dryer with shelf temperature ramped from -40°C to +20°C over 36–48 h; primary drying is controlled at -20°C ± 5°C with chamber pressure 0.2 mbar, and secondary drying at 25–30°C until residual moisture is ≤ 0.5% w/w by USP <921>. The ± 5°C primary drying window is critical because collapse of the mannitol crystalline matrix leads to loss of cake structure and reconstitution time > 2 min. After drying, stoppers are closed under vacuum or sterile nitrogen inside the chamber; crimp seals are applied outside the aseptic core. Reconstitution is performed with water for injection to 10–20 mg/mL; particulate matter after reconstitution must meet USP <788>. Terminal finished product is lyophilized powder for injection. Compliance includes EU GMP Annex 1 for closed-vial integrity, USP <1207> for container closure integrity, 21 CFR 211, ICH Q3D(R2), and ICH Q1A(R2) for freeze-dried stability. Incompatibility: primary amine groups may react with residual aldehydes from stopper steam sterilization or rubber curing; bromobutyl stoppers must be washed and autoclaved per USP <381> and tested for volatile leachables.

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    Certification & Compliance
    More Introduction

    2,3-Diaminopyridine Pharma Grade API, supplied under the manufacturer-specific model designation 2,3-DAP-PG, is a crystalline drug substance with molecular formula C5H7N3 and CAS Registry Number 452-58-4. The molecular mass is 109.13 g/mol. The material is controlled for use in oral solid dosage forms—tablets, capsules, and granules—and in injectable preparations where downstream aseptic processing or terminal sterilization is supported by validated stability data. No harmonized pharmacopoeial monograph for this exact positional isomer is published in the major compendia; release therefore follows the ICH Q6A decision tree with validated in-house high-performance liquid chromatography, infrared spectrophotometry, and residual solvent procedures. The pharma grade differs from technical-grade material primarily by a lower bacterial endotoxin limit, a restricted residual solvent profile aligned with ICH Q3C, and an impurity panel that controls the 2,6- and 3,4-isomers and related pyridine by-products.

    The API is not a finished dosage form. It is incorporated into tablets, capsules, granules, or injectable formulations only after excipient compatibility, forced degradation, and process validation. For solid oral dosage forms, the material can be blended by direct compression or granulated by high-shear wet processing. A representative oral grade may show D90 below 100 µm and bulk density in the range 0.45–0.60 g/cm³, but these values are lot-specific and must be confirmed against the manufacturer's certificate of analysis because no universal compendial particle-size limit exists. Pre-drying is required when ambient relative humidity exceeds 60%, as moisture uptake can reduce flow and cause caking in hopper feed systems. The primary amine functionalities react with reducing sugars and aldehydes; therefore, lactose-based wet granulation requires a compatibility study under 40°C/75% RH for 4 weeks before scale-up. For capsule filling, poor flow may require roller compaction or slugging. If colloidal silicon dioxide is used as a glidant, addition levels above 0.5% w/w can reduce blend compressibility and increase ejection force on single-station tablet presses.

    Specification Panel and Analytical Reference Limits

    Representative release criteria for the pharma grade are summarised below. Actual limits are manufacturer-specific and should be verified against the active drug master file or active substance master file. When a single API is used for oral and injectable products, the stricter injectable specification should govern release for microbial quality and endotoxin.

    TestRepresentative acceptance criterionAnalytical reference
    AppearanceWhite to off-white crystalline powderVisual inspection against reference standard
    IdentificationIR spectrum conforms to reference; HPLC retention time matches standardPh. Eur. 2.2.24, 2.2.29
    Assay99.0–101.0% w/w on anhydrous basisValidated HPLC with UV detection
    Related substancesTotal impurities ≤0.5%; any unspecified impurity ≤0.10%; positional isomers ≤0.15% eachValidated HPLC area normalisation
    Water0.5% w/wPh. Eur. 2.5.12
    Residue on ignition0.1%Ph. Eur. 2.4.14
    Heavy metals10 ppmPh. Eur. 2.4.8
    Residual solventsICH Q3C Option 1 limitsHeadspace GC
    Bacterial endotoxins0.05 EU/mg for injectable gradePh. Eur. 2.6.14
    Microbial limitTAMC ≤10³ CFU/g; TYMC ≤10² CFU/g for oral gradePh. Eur. 5.1.4

    For granules intended for sachet or capsule filling, fluid-bed granulation with an aqueous binder can be used when the API is pre-mixed with a hydrophilic filler. Granulation end-point should be monitored by impeller torque or power consumption rather than time alone; over-granulation increases the fraction of large agglomerates and reduces dissolution rate. The API’s amine groups can interact with acidic excipients such as citric acid. If an acidulant is required for a buffered or taste-masked formulation, a compatibility study under 40°C/75% RH for 4 weeks should be conducted to rule out salt formation or hygroscopicity collapse. The dried granulation should lie between 1.0% and 3.0% residual moisture before compression; a tablet tensile strength above 1.5 MPa and friability below 1.0% in accordance with USP <1216> are typical development targets for immediate-release tablets.

    Aseptic manufacturing of injectable dosage forms from 2,3-DAP-PG imposes a different control space. Bacterial endotoxin must be below 0.05 EU/mg, total aerobic microbial count must be controlled, and processing water must meet WFI compendial standards. Terminal sterilization at 121°C for 15 minutes may be acceptable only when supported by stress studies and pH-buffering selection; the aromatic amine is susceptible to oxidative discoloration when solution pH exceeds 7.5, so nitrogen-blanketed preparation and storage under vacuum are advised. If aseptic filtration is used, a 0.22 µm PVDF or PES membrane is preferred; nylon membranes are not recommended because the aminopyridine ring may adsorb to polyamide surfaces. For lyophilized injection, the collapse temperature must be established by freeze-drying microscopy; published data for this specific isomer is limited, so development lots require differential scanning calorimetry and residual moisture mapping. The API should be protected from light and stored in amber glass or double LDPE bags inside HDPE drums at 15–25°C.

    Why Is Regiochemistry a Control Rather Than a Cosmetic Variation?

    2,3-Diaminopyridine is a positional isomer of 3,4-diaminopyridine and 2,6-diaminopyridine. The three isomers share the same molecular formula and molecular mass, but the orientation of the amino groups changes the electronic environment of the pyridine ring, the ability to form hydrogen-bonded networks, and the interaction with polar excipients and metal surfaces. The 2,3-isomer has adjacent amino groups that can act as bidentate coordination sites; this requires the final synthetic step to exclude transition-metal catalysts and to control metal residues below the ICH Q3D limit for parenteral products. By contrast, 3,4-diaminopyridine is the active substance in amifampridine formulations for Lambert-Eaton myasthenic syndrome and has a distinct clinical and regulatory identity. 2,6-Diaminopyridine is primarily used as a synthetic intermediate and is not interchangeable with the 2,3-isomer in a licensed drug product. Batch records must therefore confirm positional isomer identity by infrared spectroscopy and a chromatographic method capable of resolving the three diaminopyridine isomers.

    Property2,3-Diaminopyridine3,4-Diaminopyridine2,6-Diaminopyridine
    CAS452-58-454-96-6141-86-6
    Molecular mass109.13 g/mol109.13 g/mol109.13 g/mol
    Substitution patternVicinal amino groups; ortho relationship1,2-diamino substitution relative to ring nitrogenSymmetric 2,6-disubstitution
    Regulatory contextNo harmonized monograph; controlled via DMF/ASMF; use restricted to authorized formulationsPharmaceutical amifampridine; clinical use in Lambert-Eaton myasthenic syndromePrimarily intermediate; not typically a drug substance
    Key control riskIsomer separation, metal residues, endotoxinIsomer impurities, genotoxic potential of related diaminesSynthetic carryover, residual catalyst

    When a Single API Grade Must Serve Oral and Injectable Routes

    If a manufacturer uses one API grade for both oral and injectable products, the injectable specification should govern release for bacterial endotoxin, microbial enumeration, and particulate matter. A dual-grade program can reduce inventory complexity but creates a conflict because oral solid dosage manufacturing often tolerates a higher bioburden and wider particle-size distribution. The conflict is resolved by applying the parenteral acceptance criterion of ≤0.05 EU/mg to every lot, even when the lot is intended only for tablet or capsule manufacture. This approach increases testing cost but prevents cross-contamination of a non-controlled lot into sterile production. In addition, the residual solvent profile must be re-evaluated for each route; solvents accepted for oral use under ICH Q3C may require tighter limits if the injectable product is manufactured with the same solvent-laden API. The cleaning validation matrix should separate oral and injectable equipment trains; use of shared granulators or bins without dedicated validation invites cross-contact with non-sterile powders and is discouraged.

    The primary aromatic amine groups of 2,3-diaminopyridine are sensitive to nitrous acid; exposure to nitrite can form diazonium intermediates, with potential genotoxic impurities. Secondary amine impurities, if present, require a nitrosamine risk assessment under ICH M7. Nitrite-containing cleaning solutions, acidic process waters with nitrate reduction, and nitroso-containing excipients must be excluded from all stages of drug product manufacture. The API should be stored away from strong oxidising agents, acid chlorides, and reducing sugars. If a tablet or capsule formulation requires a reducing sugar or an aldehyde-based flavoring agent, the compatibility data must demonstrate no Schiff base formation and no increase in related substances beyond the specified limit. The API is not intentionally sterile; injectable formulations require further aseptic processing or terminal sterilization. Published data for this specific isomer in parenteral formulations is limited; therefore, each manufacturer should generate in-use stability data in the intended diluent and primary packaging.

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