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

    • Product Name: Hesperidine 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 872361
    Product Name Hesperidine (Hesperidin) Pharma Grade API
    Synonyms Hesperidin, Cirantin, Hesperetin 7-rutinoside, Vitamin P, Hesperidine
    Cas Number 520-26-3
    Molecular Formula C28H34O15
    Molecular Weight 610.56 g/mol
    Appearance Light yellow to off-white crystalline powder
    Assay Purity 90.0% to 95.0% (HPLC)
    Grade Pharma Grade / API Grade
    Dosage Forms Tablet, Capsule, Granule, Injection, Oral, Injectable
    Route Of Administration Oral and Injectable
    Solubility Practically insoluble in water; soluble in dimethyl sulfoxide and aqueous alkaline solutions
    Storage Conditions Store in a cool, dry, well-ventilated area, protected from light and moisture
    Shelf Life 24 months when stored as recommended
    Packaging 25 kg fiber drum with double polyethylene inner bags; customizable packaging available
    Pharmacopoeia Standard USP/EP/BP/JP or in-house specification
    Hs Code 29389090
    Manufacturing Process Extraction from citrus fruits and purification
    Quality Control HPLC, GC, ICP-MS, microbial testing, heavy metals testing
    Supply Ability Commercial quantities available

    As an accredited Hesperidine 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 Hesperidine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Pharma-grade hesperidine API, supplied as the flavanone glycoside hesperidin (CAS 520-26-3, molecular weight 610.56 g/mol), enters oral solid dosage manufacturing most commonly as the minor active component of micronized purified flavonoid fraction (MPFF) used in venotonic therapy. The most demanding direct application is an immediate-release film-coated tablet for chronic venous insufficiency and hemorrhoidal disease, in which the addition ratio is controlled at 450 mg diosmin plus 50 mg hesperidin per 500 mg active fraction, corresponding to 90:10 w/w diosmin:hesperidin and 6.25% w/w hesperidin in an 800 mg uncoated tablet core. The reason this formulation is rarely compressed directly is that micronized hesperidin with a laser-diffraction d90 below 10 µm produces a cohesive powder bed showing angle of repose above 40° and Carr index above 25%, conditions that on a rotary tablet press with B-tooling 9 mm round concave punches at 12–20 kN compression force cause feed frame blockage, weight variation, and capping. Production therefore uses wet granulation: a top-drive high-shear granulator blends the active fraction with microcrystalline cellulose and pregelatinized starch at impeller speed 180–250 rpm and chopper speed 1200–1800 rpm, adds a 5% w/w povidone K30 binder solution, discharges the wet mass through a 1.0 mm screen, dries it in a fluid-bed dryer at 55–65 °C inlet air until loss on drying is NMT 2.5%, and sieves the granulate through 0.8 mm mesh. Extragranular croscarmellose sodium at 2.0–4.0% w/w and magnesium stearate at 0.5% w/w are added before compression, and an aqueous HPMC-based film coating is applied to 2.0–3.0% weight gain in a perforated pan coater. The compliance frame includes Ph.Eur. monographs for diosmin and hesperidin, USP <905>/Ph.Eur. 2.9.40 for uniformity of dosage units, USP <711>/Ph.Eur. 2.9.3 for dissolution, USP <621>/Ph.Eur. 2.2.29 for HPLC assay, ICH Q3C for residual solvents, and ICH Q3D for elemental impurities. The terminal finished product type is a biconvex film-coated tablet for oral administration.

    Hard Capsule Direct Fill Fails Without Forced-Feed Control When Bulk Density Drops Below 0.45 g/mL

    Direct encapsulation of hesperidin powder into hard gelatin or HPMC capsules is typically limited to monotherapy or low-active-mass formulations because the API has an irregular platelet-like morphology and low bulk density; when bulk density falls below 0.45 g/mL, dosator-type capsule filling machines without forced-feed auger agitation commonly show fill weight RSD above 4.0%, undermining the USP <905> acceptance value L1 ≤ 15.0. In a representative size 1 capsule with 250 mg total fill mass, the addition ratio of 100 mg hesperidin per capsule is 40.0% w/w, with microcrystalline cellulose at 50.0% w/w, pregelatinized starch at 8.0% w/w, colloidal silicon dioxide at 1.0% w/w, and magnesium stearate at 0.5–1.0% w/w; this formula must be verified by stratified blend uniformity sampling at 10 locations before machine start-up. The downstream process consists of dry pre-blending in a bin blender at 12–18 rpm for 15–20 minutes, screening through a 0.6 mm sieve, final lubrication for 3–5 minutes, and encapsulation on a dosator machine fitted with forced-feed auger agitation; capsule fill weight and closure are monitored at 15-minute intervals. Disintegration is tested against USP <701>/Ph.Eur. 2.9.1 in water at 37 ± 2 °C with a limit of NMT 15 minutes, and dissolution is tested against USP <711>/Ph.Eur. 2.9.3 using a validated immediate-release medium. The terminal finished product type is a hard gelatin or HPMC capsule for oral administration.

    What Limits Dispersion Stability and Sieve Uniformity in Hesperidin Granules for Sachet Reconstitution?

    In granule/sachet production, the central process conflict is that reducing hesperidin particle size to improve dissolution rate simultaneously increases interparticle cohesion and the risk of overwetting or balling during high-shear granulation. For a 1,500 mg total granule fill mass per sachet containing 1,000 mg micronized purified flavonoid fraction, the hesperidin addition ratio is 100 mg per sachet, or 6.67% w/w of the total granule mass, when the active fraction is controlled to 90:10 w/w diosmin:hesperidin. The manufacturing process uses a top-drive high-shear granulator with impeller speed 200–300 rpm and chopper speed 1,400–1,800 rpm; purified water or a 5% w/w povidone K30 solution is sprayed at 15–25 g/min per kg dry powder until the granule mean size falls within 150–300 µm. The wet granules are transferred to a fluid-bed dryer with inlet air at 55–65 °C until residual moisture is NMT 2.0%, passed through an 0.8 mm oscillating sieve, and finally passed through a 0.315 mm sieve to control fines below 10% w/w. Dispersion quality is evaluated by reconstituting one sachet in 100 mL water at 20 ± 2 °C with manual stirring for 30 seconds; the dispersion must pass through a 0.315 mm screen without retained lumps. The compliance frame includes Ph.Eur. 2.9.40/USP <905> for content uniformity, Ph.Eur. 2.9.1/USP <701> for disintegration where applicable, USP <711>/Ph.Eur. 2.9.3 for dissolution, and ICH Q3B for degradation products. The terminal finished product type is a single-dose sachet containing granules for oral suspension.

    When Injectable Hesperidin Is Developed for Lyophilized Powder Reconstitution, Solubility and Sterility Metrics Control the Process

    Hesperidin is practically insoluble in water with published solubility values generally below 5 mg/L at 25 °C; injectable dosage forms therefore require a solubilisation strategy such as hydroxypropyl-β-cyclodextrin complexation or pH-adjusted co-solvent systems, and the addition ratio must be derived from phase-solubility data rather than a fixed pharmacopoeial formula. A representative lyophilised vial formula may contain 20 mg hesperidin, 200–400 mg hydroxypropyl-β-cyclodextrin, and 40–80 mg mannitol per 10 mL vial, giving a hesperidin-to-cyclodextrin mass ratio of 1:10 to 1:20 w/w; after reconstitution with 5 mL water for injection, the nominal hesperidin concentration is 4.0 mg/mL. The downstream process includes dissolution in nitrogen-sparged water for injection at 40–60 °C for 2–4 hours, cooling to 20–25 °C, pH adjustment to 6.5–7.5 with diluted sodium hydroxide or hydrochloric acid, sterile filtration through a 0.22 µm polyethersulfone membrane, filling into depyrogenated glass vials, and lyophilisation with shelf freezing at −40 °C, primary drying at −20 °C to −10 °C under 0.1–0.2 mbar for 24–48 hours, and secondary drying at 20–25 °C until residual moisture is NMT 2.0%. In-process controls include filter integrity testing, bioburden before filtration, USP <71>/Ph.Eur. 2.6.1 sterility, USP <85>/Ph.Eur. 2.6.14 bacterial endotoxins, USP <788>/Ph.Eur. 2.9.19 subvisible particulate matter, and ICH Q3C residual solvent limits. Published data for commercial hesperidin injection formulations is limited; therefore, the exact addition ratio and lyophilisation cycle must be established through development batches and design-of-experiment studies. The terminal finished product type is a sterile lyophilized powder for injection after reconstitution.

    Compendial control framework for hesperidin oral and injectable dosage forms
    Control parameterMethod / standardNumerical acceptance window
    HPLC assay of hesperidinUSP <621> / Ph.Eur. 2.2.29System suitability RSD ≤ 2.0%; tailing factor ≤ 2.0
    Uniformity of dosage unitsUSP <905> / Ph.Eur. 2.9.40L1 ≤ 15.0 for oral solid dosage forms
    Dissolution, immediate-release oral formsUSP <711> / Ph.Eur. 2.9.3Q = 80% at 30 minutes; stage S1 to S3
    Disintegration of tablets/capsulesUSP <701> / Ph.Eur. 2.9.1NMT 15 minutes in water at 37 ± 2 °C
    Subvisible particles for reconstituted injectionUSP <788> / Ph.Eur. 2.9.1910 µm NMT 6000 per container; ≥ 25 µm NMT 600 per container
    Elemental impuritiesICH Q3DOral Pb NMT 5 µg/day, Cd NMT 2 µg/day, As NMT 15 µg/day, Hg NMT 4 µg/day
    Residual solventsICH Q3CClass 2 methanol NMT 3000 ppm; Class 3 ethanol NMT 5000 ppm

    Direct compression monotherapy tablets become a viable route only when the hesperidin mass fraction is kept low enough to avoid the flow and compactibility failures observed in high-dose MPFF tablets. In a 200 mg tablet core containing 50 mg hesperidin, the addition ratio is 25.0% w/w; the bulk diluent is a coprocessed microcrystalline cellulose–lactose monohydrate filler at 65.0% w/w, crospovidone at 5.0% w/w, colloidal silicon dioxide at 1.0% w/w, and sodium stearyl fumarate at 1.0% w/w. The process uses a bin blender at 15–20 rpm for 12–18 minutes, followed by compression on a rotary tablet press with 8 mm round flat-faced bevel-edge punches at 8–14 kN compression force and turret speed 25–50 rpm. Hardness is maintained at 60–100 N, friability is NMT 1.0% after 100 drum revolutions, thickness is 3.0–3.6 mm, and disintegration is tested according to USP <701>/Ph.Eur. 2.9.1 in water at 37 ± 2 °C for NMT 15 minutes. The compliance frame includes USP <905>/Ph.Eur. 2.9.40 for uniformity of dosage units, USP <711>/Ph.Eur. 2.9.3 for dissolution, USP <621>/Ph.Eur. 2.2.29 for assay, and ICH Q3D for elemental impurities. The terminal finished product type is an uncoated or film-coated immediate-release tablet for oral administration.

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    Certification & Compliance
    More Introduction

    Hesperidine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is supplied as a flavanone glycoside with the chemical identity hesperetin-7-O-rutinoside and CAS registry number 520-26-3. The molecule has a relative molecular mass of 610.56 g/mol, with the formula C28H34O15, and is released as a crystalline or microcrystalline powder. No harmonised model nomenclature exists across manufacturers; certificates of analysis instead carry grade codes linked to assay, particle-size distribution, residual solvent class, and endotoxin claim. Oral grades are commonly designated by a D90 value in the range 50–100 µm, while injectable grades are released as micronized material with a D90 typically ≤ 10 µm. The designations “micronized” and “sterile-filterable” on supplier documentation therefore describe performance attributes rather than a universal model number.

    Why Does Particle Size Control Define Tablet and Capsule Performance?

    Because hesperidine is practically insoluble in water, dissolution rate rather than solubility equilibrium governs release from solid oral dosage forms. Particle-size reduction to a D90 of ≤ 50 µm is specified for tablets and capsules where immediate release is intended; for granules, retention of some larger agglomerates is acceptable if the granule disintegrates rapidly. Direct compression of unmilled API is not recommended; low bulk density and poor flow create weight variation and capping. In production-scale trials, tablets containing greater than 30% w/w unmilled hesperidine have exhibited capping at compression forces above 15 kN; roller compaction or high-shear wet granulation mitigates this. Dissolution testing per USP <711> typically requires a surfactant-containing medium; 0.5% w/v sodium lauryl sulfate in phosphate buffer at pH 6.8 is used to discriminate batches with inadequate particle-size control. Air-jet milling and pin milling are preferred over hammer milling because they reduce the formation of amorphous surface domains that recrystallise during storage.

    Pharmacopoeial Release Criteria and Analytical Markers

    Release control relies on orthogonally selective methods. Where a pharmacopoeial monograph for hesperidin is applied, assay and related substances are determined by reversed-phase HPLC; where no monograph is available in a given jurisdiction, supplier methods aligned with Ph. Eur. 2.2.29 and USP <621> are accepted provided they are shown to be stability-indicating. The representative release criteria in Table 1 apply to oral and injectable grades, with the injectable grade subject to additional endotoxin and sterility controls.

    ParameterRepresentative release criterionMethod alignment
    AppearancePale yellow to light brown crystalline powderVisual inspection
    IdentificationIR spectrum matches reference; HPLC retention time matches standardPh. Eur. 2.2.24, 2.2.29
    Assay95.0–102.0% on dried basisHPLC, Ph. Eur. 2.2.29 / USP <621>
    Total related substances≤ 2.0%HPLC, area normalisation
    Loss on drying≤ 5.0%Ph. Eur. 2.2.32
    Sulfated ash≤ 0.1%Ph. Eur. 2.4.14
    Elemental impuritiesLimits per ICH Q3DUSP <232>/<233>, Ph. Eur. 2.4.20
    Residual solventsConforms to ICH Q3C limitsPh. Eur. 2.4.24 / USP <467>
    Particle size, oralD90 ≤ 100 µmLaser diffraction, Ph. Eur. 2.9.31 / USP <429>
    Particle size, injectableD90 ≤ 10 µmLaser diffraction, Ph. Eur. 2.9.31 / USP <429>
    Microbial limitsTAMC ≤ 10³ CFU/g, TYMC ≤ 10² CFU/g, E. coli absentPh. Eur. 5.1.4 / USP <61>, <62>
    Bacterial endotoxins, injectable≤ 0.25 EU/mg or lower based on maximum dosePh. Eur. 2.6.14 / USP <85>
    Sterility, injectableMeets testPh. Eur. 2.6.1 / USP <71>

    For assay and related substances, a stability-indicating reversed-phase HPLC method is used with an octadecylsilane column of 150 mm × 4.6 mm, 5 µm particle size, operated at 30°C. Detection at 280–284 nm and gradient elution using acidified aqueous methanol are typical. The method must resolve hesperidine from the isomeric flavanone neohesperidin, if present, with a resolution of ≥ 2.0, tailing factor ≤ 1.5, and injection precision ≤ 2.0% RSD. Residual solvents in commercial hesperidine are primarily methanol and ethanol from citrus peel extraction and subsequent purification. Methanol is controlled to ≤ 3000 ppm and ethanol to ≤ 5000 ppm unless a supplier-specific limit is justified under ICH Q3C.

    Regulatory submissions for oral tablets and capsules typically reference the same API release data, but granule formulations may require additional sieve-distribution data after blending. For injectable products, the drug substance section of the dossier must include endotoxin method validation and compatibility data with the chosen solubilising excipient. Where a CEP or US DMF is used, the applicant is responsible for demonstrating that the dosage-form manufacturing process does not introduce new impurities above qualification thresholds under ICH Q3B; storage below 25°C and protected from light is required within the re-test period.

    When the Oral Grade Is Transferred to High-Shear Granulation Lines

    When the oral grade is processed on high-shear granulation equipment, the low aqueous solubility and hygroscopic character of hesperidine create a narrow processing window. In a bowl of 300–600 L working capacity, representative processing conditions for this class of flavanone glycoside include a wet-massing time of 4–6 min at an impeller tip speed of 10 m/s; longer massing produces denser granules that later fail dissolution specifications. The granules exhibit a bimodal particle-size distribution and hard agglomerates when the water/binder ratio exceeds 18–22% w/w. Subsequent drying in a fluid-bed dryer with product temperature above 65°C accelerates oxidative discolouration, so exhaust air temperature is controlled at 55–60°C. In production batches, end-of-drying LOD is set at ≤ 2.5% w/w for tablet compression and ≤ 3.5% w/w for capsule filling to avoid picking and caking. The dried granulate is milled through a 1.0 mm conical screen and blended with external disintegrant to restore disintegration time below 15 min in pH 6.8 phosphate buffer with 0.5% w/v sodium lauryl sulfate as per USP <711>. If dry granulation is selected, roller compaction with a gap of 2.0 mm and a roll pressure of 80–120 bar is used; ribbons are milled at 500 rpm to produce granules with a bulk density suitable for encapsulation.

    Granule sachet formulations are distinct from tablets because they are reconstituted in water before administration. Hesperidine remains suspended rather than dissolved; particle size after reconstitution must remain below 500 µm to avoid mouthfeel defects and dosing variability. Wet granulation with mannitol or sorbitol provides dispersibility, but hygroscopic exposure above 60% RH causes the granules to agglomerate in aluminium-foil sachets. A desiccant is therefore included when the sachet barrier is not fully aluminium-laminated.

    Terminal Sterilisation Is Not the Default Route for Hesperidine Injectables

    Injectable-grade hesperidine is released only after additional purification to reduce endotoxin and bioburden. The API itself is practically insoluble in water; aqueous formulations require a co-solvent system, cyclodextrin complexation, or phospholipid/surfactant micellar solubilisation. Sterile filtration through a 0.22 µm PVDF or PES membrane is feasible only when the drug is fully solubilised and the solution has low viscosity. A 0.45 µm prefilter is placed upstream to prevent premature fouling. Terminal sterilisation at 121°C for 15 min may be used only after forced-degradation studies demonstrate a shelf-life-acceptable loss of assay; if the aqueous formulation shows degradation above 2% or colour shift, aseptic filtration is required. The injectable-grade API must meet Ph. Eur. 2.6.14 / USP <85> for bacterial endotoxins and Ph. Eur. 2.6.1 / USP <71> for sterility. Avoid combination with strong bases and strong oxidising agents because the phenolic hydroxyls at positions 5 and 3’ undergo oxidative coupling and ring scission. Published data for this specific configuration is limited.

    The oral grade is not interchangeable with the injectable grade. Oral-grade material may display endotoxin levels and viable counts that are acceptable for solid-dose manufacture but fail parenteral limits. Injectable-grade material is typically further processed by solvent recrystallisation, activated-carbon treatment, or ultrafiltration to reduce high-molecular-mass polyphenolic aggregates; these operations narrow the impurity profile but can increase cost and reduce yield. In lyophilised injectable formulations, mannitol or trehalose is used as a bulking agent at 4–6% w/v; the hesperidine concentration is limited by the solubility of the selected cyclodextrin or co-solvent system rather than by the dry powder itself.

    Comparing Hesperidine with Diosmin, Hesperetin, and Rutin

    Hesperidine, diosmin, hesperetin, and rutin are related polyphenolic substances with divergent formulation behaviour. Hesperidine is a flavanone 7-O-rutinoside; diosmin is the corresponding flavone 7-O-rutinoside and differs by oxidation at the C2–C3 bond. Hesperetin is the aglycone with a relative molecular mass of 302.28 g/mol and crosses biological membranes more readily, but its lower glycosidic mass reduces the hydrophilicity advantage of the parent glycoside. Rutin, a flavonol 3-O-rutinoside, has a relative molecular mass of 610.52 g/mol and a different oxidation profile. In solid-dose processing, diosmin is frequently more electrostatic and requires wet granulation; hesperetin has higher log P and may require lipid excipients; rutin is more hydrophilic but degrades rapidly at pH above 8. Table 2 summarises the comparative formulation constraints.

    SubstanceChemical classRelative molecular massAqueous solubility profileSolid-dose consequence
    HesperidineFlavanone 7-O-rutinoside610.56 g/molPractically insoluble; dissolution-rate limitedMicronization or roller compaction; avoid direct compression.
    DiosminFlavone 7-O-rutinoside608.54 g/molPractically insoluble; electrostatic in dry blendingWet granulation; antistatic humidification.
    HesperetinFlavanone aglycone302.28 g/molPractically insoluble; higher membrane permeabilityLipid-based excipients; oxidation control.
    RutinFlavonol 3-O-rutinoside610.52 g/molVery slightly soluble in water; pH-sensitivepH-stabilised granulation; light protection.

    Selection of an oral or injectable grade of hesperidine is therefore governed by the downstream unit operations and microbiological requirements. The oral grade is accepted for tablets, capsules, and granules where particle size, LOD, and residual solvent limits are controlled; the injectable grade is used only after endotoxin, sterility, and sub-visible particulate testing. In both cases, the API must be protected from light in amber glass or opaque polyethylene-lined drums, stored below 25°C, and quarantined until HPLC assay, moisture, and impurity results conform to the release specification. Avoid contact with strong oxidising agents, and avoid processing in high-humidity environments exceeding 60% RH without pre-drying.

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