Products

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

    • Product Name: Lamivudine 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 797287
    Product Name Lamivudine Pharma Grade API
    Suitable Dosage Forms Tablet, Capsule, Granule, Injection (Oral and Injectable)
    Cas Number 134678-17-4
    Molecular Formula C8H11N3O3S
    Molecular Weight 229.26 g/mol
    Chemical Name 4-Amino-1-[(2R,5S)-2-(hydroxymethyl)-1,3-oxathiolan-5-yl]pyrimidin-2-one
    Appearance White to off-white crystalline powder
    Solubility Freely soluble in water; sparingly soluble in methanol; practically insoluble in acetone
    Assay On Dried Basis 99.0% to 101.0%
    Specific Optical Rotation -97.0° to -107.0°
    Melting Range 160°C to 166°C
    Residual Solvents Complies with ICH limits
    Storage Condition Store in a tightly closed container, protected from moisture and light, at controlled room temperature

    As an accredited Lamivudine 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 Lamivudine Pharma Grade API packaged in sealed, double-lined drums, 25 kg net per drum, labeled for safe oral and injectable formulation use.
    Container Loading (20′ FCL) One 20-foot FCL container of Lamivudine pharma-grade API, securely packed, temperature-controlled, for oral and injectable pharmaceutical manufacturing.
    Shipping Lamivudine Pharma Grade API is shipped in sealed, moisture-proof containers to preserve potency and stability. Export packaging complies with international pharmaceutical regulations, with full documentation for customs clearance. Secure global courier dispatch ensures timely, traceable delivery for tablet, capsule, granule, injection, and oral/injectable manufacturing.
    Storage Store Lamivudine Pharma Grade API in tightly sealed, original containers in a cool, dry, well-ventilated area at controlled room temperature, protected from light, moisture, and heat. Keep away from incompatible substances and food. Ensure proper labeling and secure access. Avoid prolonged exposure to air; use according to handling guidelines.
    Shelf Life Shelf life is typically 24 to 36 months when stored under recommended conditions in original, sealed containers.
    Application of Lamivudine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Lamivudine as a single-agent pharmaceutical-grade API is processed into 150 mg and 300 mg film-coated tablets for oral antiretroviral administration. The addition ratio is controlled on a per-unit basis rather than through a universal percentage: each tablet contains 150 mg or 300 mg of lamivudine, with release testing anchored to an assay window of 90.0–110.0% of the label claim under USP Lamivudine Tablets and uniformity of dosage units under USP <905>. The powder blend is manufactured in a 200 L bin blender at 12–18 rpm for 10–15 min; segregation is minimized when the API particle size distribution is kept with d90 below 250 µm. Precompression bulk density must be measured because lamivudine is a high-dose API and can generate punch capping if the active ratio exceeds roughly 40–50% w/w in brittle filler systems; if the API is received as micronized powder, the material is first dry granulated on a roller compactor at 8–12 kN/cm roll force and milled to 16–20 mesh before final blending. Core compression on a 45-station rotary tablet press at 60–80 rpm with a main compression force of 10–18 kN typically yields hardness of 60–90 N and friability under USP <1216> below 1.0%.

    Aqueous film coating follows in a 48-inch perforated coating pan; the coating suspension contains hypromellose, polyethylene glycol, and titanium dioxide. Inlet air temperature is set at 60–70 °C and the spray rate is adjusted to keep product bed temperature between 40 °C and 45 °C; this balance prevents overwetting and logo bridging while yielding a 3–5% w/w weight gain. Downstream packaging with aluminum/aluminum cold-form blisters must control residual moisture below 2.0% because the core contains a superdisintegrant and may soften under high relative humidity. Industry compliance for the finished product is established under FDA 21 CFR 210 and 211, with elemental impurity limits per ICH Q3D and residual solvent thresholds per ICH Q3C. Terminal finished products are single-agent lamivudine film-coated tablets at 150 mg and 300 mg strengths for oral HIV therapy.

    What Formulation Constraints Arise When Lamivudine Is Co-Compressed with Dolutegravir and Tenofovir Disoproxil Fumarate?

    In fixed-dose combination tablets, lamivudine is added at 300 mg per unit with tenofovir disoproxil fumarate 300 mg and dolutegravir 50 mg per unit; this triple combination is processed as a layered or homogenized compression based on segregation risk. The downstream process typically begins with separate pre-blends because the API particle sizes and bulk densities differ: tenofovir disoproxil fumarate has poor flow and is densified through dry granulation, while lamivudine and dolutegravir may be wet granulated with a 5% w/w povidone binder solution in a 250 L high-shear granulator at an impeller speed of 120–180 rpm and chopper speed of 1500–3000 rpm. The wet mass is dried in a fluid-bed dryer at an inlet air temperature of 55–65 °C to a final loss-on-drying of 1.5–2.5%; the dried granulate is milled through a 1.0 mm screen. Compression on a 37-station rotary press must be run in contained isolation because of the occupational exposure limits of the integrase inhibitor; main compression force is set between 15 kN and 25 kN to maintain tablet hardness above 100 N.

    Compliance is anchored to ICH Q8(R2) design space and FDA 21 CFR 211.110 in-process sampling; finished product assay must meet 90.0–110.0% for each API. Dissolution is performed using USP <711> with product-specific media and paddle speed; the fast-release behavior of lamivudine can mask slower-release fractions of the companion APIs, so a two-stage or media-pH gradient may be required to discriminate failed batches. The tablet mixture must also meet a pharmacopoeial uniformity limit of AV ≤ 15 under USP <905> across the batch. Table 1 compares three marketed fixed-dose patterns in which lamivudine is present under different co-API loads.

    Fixed-dose patternLamivudine addition per unitCo-formulated APIsPrimary process constraint
    Lamivudine/zidovudine150 mgZidovudine 300 mgHigh-dose dual API blending; segregation control
    Abacavir/lamivudine300 mgAbacavir sulfate equivalent to 600 mg abacavirHigh tablet mass; dissolution interference between APIs
    Dolutegravir/lamivudine/tenofovir disoproxil fumarate300 mgDolutegravir 50 mg; tenofovir disoproxil fumarate 300 mgLow-dose uniformity risk for dolutegravir; flow differences

    At an addition level of 150 mg or 300 mg per capsule, lamivudine is filled into hard gelatin or hypromellose capsule shells after a direct-blend or slugged granulation process. The final blend must meet a content uniformity acceptance value of AV ≤ 15 under USP <905>, and the filling operation on a dosator-type capsule machine at 50,000–80,000 capsules/hour is limited by powder flow rather than by API solubility. A fill mass of 450 mg containing 150 mg lamivudine corresponds to 33.3% w/w active; for the 300 mg strength, the fill mass is adjusted upward to 500–650 mg, depending on excipient density. Compliance is governed by 21 CFR 211 and ICH Q3D elemental impurity limits; terminal product type is an oral capsule used principally in clinical trial blinding, alternate supply, or patient-specific compounding where tablets are unsuitable.

    Pediatric Oral Granule Reconstitution and Bitter-Masking Particle Coating

    Lamivudine-containing granules for pediatric oral administration are produced to a reconstituted concentration of 10 mg/mL, equivalent to 1.0% w/v in the final liquid. The granular intermediate is manufactured by top-spray fluid-bed granulation in which lamivudine is blended with a water-soluble filler such as mannitol and a suspending agent such as xanthan gum; binder solution, typically povidone or hydroxypropyl cellulose at 5% w/w, is sprayed at 10–20 g/min onto a product bed maintained at 35–45 °C. The granulation endpoint is defined by particle size distribution: 90% of particles between 150 µm and 710 µm to ensure rapid reconstitution without floating. A secondary lipid-polymer coating is applied to suppress the bitter taste of lamivudine; this coating increases particle diameter by 15–25 µm and delays dissolution in artificial saliva by 30–60 seconds, which is sufficient for organoleptic masking but does not impair release in 0.1 N HCl medium.

    Compliance is established under EMA/CHMP pediatric formulation guidance, ICH Q3B degradation product thresholds, and USP <905> for unit dose uniformity of the dry powder. The reconstituted suspension is filled into 100 mL HDPE bottles with child-resistant closures, and the terminal product type is an oral granule/powder for suspension for pediatric HIV or HBV treatment. Published data for the exact marketed granule composition is limited; in-house development batches should verify sedimentation volume and redispersibility after 7 days of storage at 25 °C/60% RH.

    When Sterile Compounding Requires Lamivudine Injectable Solutions in Hospital Pharmacy Isolators

    Injectable lamivudine is not a globally registered single-agent parenteral product; published data for this specific configuration is limited. Hospital central intravenous admixture services that prepare lamivudine infusions from pharmaceutical-grade API must operate under EU GMP Annex 1 and USP <797> pharmaceutical compounding standards. A typical experimental admixture concentration is 1.5 mg/mL, created by dissolving 150 mg lamivudine in 100 mL normal saline or dextrose 5% injection under aseptic conditions. The manufacturing sequence includes sterile filtration through a 0.22 µm polyethersulfone or polyvinylidene difluoride filter and terminal filling into type I borosilicate glass vials or polypropylene infusion bags. If terminal steam sterilization is employed, the formulation must withstand 121 °C for 15 min; otherwise the product is aseptically processed in an ISO 14644-1 Class 5 isolator.

    Quality control for the injectable format demands bacterial endotoxin levels below USP <85> acceptance limits, sterility per USP <71>, and particulate matter counts meeting USP <788> for subvisible particles. The pH is adjusted to 5.0–7.0 with 0.1 N hydrochloric acid or sodium hydroxide, and osmolality is matched to blood using sodium chloride. Terminal product type is an injectable solution for institutional use only; because no harmonized pharmacopoeial monograph for lamivudine injection exists, each batch must be validated under ICH Q2(R2) for assay, purity, and preservative content if preservative is included in multidose containers.

    Injectable quality parameterStandard designationMethod condition
    SterilityUSP <71>Membrane filtration or direct transfer
    Bacterial endotoxinUSP <85>Kinetic chromogenic LAL
    Subvisible particulate matterUSP <788>Light obscuration; particle thresholds at ≥10 µm and ≥25 µm
    Visible particulate matterUSP <790>Visual inspection

    The 100 mg Hepatitis B Monotherapy Core and Its Dissolution Boundary

    Lamivudine for chronic hepatitis B is formulated as a 100 mg tablet; the lower active load permits direct compression without the high-dose segregation risks seen in HIV-strength tablets. The addition ratio in a 400 mg core is 25.0% w/w; using a 300 mg core gives 33.3% w/w. The process begins with a low-shear tumble blend of lamivudine with microcrystalline cellulose, sodium starch glycolate, and magnesium stearate; the lubricant is added at 0.5–1.0% w/w and mixed for 3–5 min to avoid over-lubrication. Compression on a 27-station rotary press at 40–60 rpm with a main compression force of 8–12 kN produces cores with hardness 40–70 N; film coating with hypromellose provides a 2–4% w/w weight gain.

    The critical release attribute is dissolution: a product-specific USP <711> test with 900 mL of 0.1 N HCl and paddle speed 75 rpm typically requires not less than 80% dissolved at 30 min. Because lamivudine is highly soluble, batch failures often reflect tablet hardness or coating thickness rather than API solubility; hardness above 90 N or coating weight gain above 6% w/w may suppress early dissolution. Compliance includes USP <905>, ICH Q3D, and residual solvents testing under ICH Q3C; terminal product type is a film-coated tablet of 100 mg for oral hepatitis B therapy.

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    Certification & Compliance
    More Introduction

    Lamivudine pharma grade API, CAS 134678-17-4, is the (−)-enantiomer of 2′,3′-dideoxy-3′-thiacytidine with molecular formula C8H11N3O3S and relative molecular mass 229.26 g/mol. The material is supplied as a white to almost white crystalline powder and is released under harmonized specifications aligned with Ph. Eur. 10.8, USP-NF, and BP monographs. The product model is defined by the intended route of administration rather than by a different chemical entity: oral-grade and injectable-grade lamivudine share the same molecular structure but differ in post-crystallization processing, environmental monitoring, packaging, and release testing. Non-micronized, micronized, and sterile-milled presentations are the commercial sub-types. The API is intended for formulation into immediate-release tablets, powder-filled hard capsules, granules for reconstitution, oral solutions, and sterile injectable preparations. Manufacturing is conducted under ICH Q7 GMP conditions with batch genealogy, change control, and documentation consistent with 21 CFR 211 for downstream finished dosage form use. Regulatory support is provided through a Certificate of Suitability or Active Substance Master File dossier. The material is synthetic; no animal-derived raw materials are introduced in the registered process, and the viral safety position is supported by the absence of human or animal excipients in the API manufacturing stream.

    Parameter Acceptance basis Method or standard
    Appearance White to almost white powder Visual examination against reference
    Identification Infrared spectrum concordant with reference; HPLC retention time concordant Ph. Eur. 2.2.24, 2.2.29, USP <197>
    Assay on dried basis 98.0% to 102.0% HPLC with external standard
    Related substances Specified impurities per monograph; unspecified impurities per ICH Q3A for maximum daily dose ≤ 2 g/day, typically ≤ 0.10% or 1 mg daily intake, whichever is lower HPLC-UV, octadecylsilyl column
    Residual solvents Class 1 solvents absent; Class 2 and Class 3 controlled per ICH Q3C Headspace gas chromatography with flame ionisation detection
    Elemental impurities Risk-assessed limits per ICH Q3D, USP <232>, Ph. Eur. 5.20 Inductively coupled plasma mass spectrometry
    Particle size D10, D50, D90 as customer specification for direct compression, granulation, or oral solution Laser diffraction per ISO 13320 or USP <429>
    Endotoxin for injectable grade Limit calculated from maximum intended dose per kilogram USP <85>, Ph. Eur. 2.6.14
    Sterility if sterile API is claimed No microbial growth USP <71>, Ph. Eur. 2.6.1

    How Does Particle Size Distribution Shift the Tablet Dissolution Window?

    Direct compaction behaviour is controlled by the interaction between particle size distribution, bulk density, and flow function. For tablet manufacture, lamivudine is not typically compressed alone; it is blended with fillers, disintegrants, and lubricants. In low-dose tablets the API weight fraction may be below 25% w/w, so segregation is controlled by geometric dilution and sieve calibration. Particle size distribution is measured by laser diffraction according to ISO 13320 or USP <429>, with D10, D50, and D90 reported on the certificate of analysis. Micronized grade is processed through an air-jet mill or pin mill, and the resulting specific surface area is characterised by Brunauer–Emmett–Teller nitrogen adsorption per ISO 9277 when required. Formulation development batches are compressed on a rotary tablet press with a force feeder and precompression station. Tablet hardness, friability, and disintegration are monitored according to USP <1217>, USP <1216>, and USP <701>. Dissolution testing is run with USP <711> Apparatus II at 37 ± 0.5 °C in media selected from pH 1.2, pH 4.5, and pH 6.8. Published compression data for pure lamivudine alone are limited; therefore, tablet process windows are established using compaction simulators at defined compaction pressures and punch velocities rather than by direct scale-up from raw powder flow measurements. Batch-to-batch variance in particle size distribution is a recognised processing bottleneck on production lines; if micronization is not controlled, direct compression can produce weight variation outside USP <905> due to segregation in the hopper or feed frame.

    For hard capsules, the powder blend is filled with a dosator or tamping-pin capsule filler. Flow, bulk density, and particle size distribution are critical because low-dose lamivudine formulations may contain 90% or more filler. Pre-blending with a glidant such as colloidal silicon dioxide improves flow, but excessive glidant can reduce blend wettability and prolong disintegration. Capsule fill weight is controlled by USP <905>, and disintegration is evaluated by USP <701>.

    Where dry blending cannot meet content uniformity requirements, wet granulation with a high-shear mixer and fluid-bed drying is used. The API is dissolved or suspended in an aqueous binder solution; because lamivudine has pH-dependent aqueous solubility, the granulation fluid is adjusted to the target pH range and the binder is selected from polyvinylpyrrolidone or hypromellose systems. Low-shear mixing should not be extended beyond the endpoint because overwetting produces hard granules and increases fines during dry milling. Drying in a fluid-bed dryer at controlled inlet air temperature is monitored by loss-on-drying and granule moisture content. Milled granules are blended with disintegrant and lubricant; lubricant blending time is kept below the threshold that causes film coating of lamivudine particles and slows dissolution in USP <711> testing.

    Sterile Injectable Grade Requirements and Endotoxin Control

    Sterile injectable presentations require more than chemical purity. The API must meet bioburden limits before terminal sterilisation or aseptic filling. If terminal sterilisation is not feasible for the finished product, the API is dissolved in Water for Injection, filtered through a sterilising-grade 0.22 µm membrane, and filled aseptically. Endotoxin limits are calculated from the maximum dose per kilogram and are verified using Ph. Eur. 2.6.14 or USP <85>. Particulate matter in the finished injection is controlled according to USP <788> or Ph. Eur. 2.9.19. The solution is adjusted to a pH compatible with injectable excipients; pH is measured with Ph. Eur. 2.2.3. For injectable grade, visible and subvisible particulate matter are controlled, and the API is packaged in low-particulate containers with double-bag protection. Process validation includes bacterial retention challenge tests for the sterilising-grade filter, media fills, and stability under ICH Q1A(R2). The injectable grade is not necessarily sterile API; it is a low-bioburden material suited for terminal sterilisation or aseptic filtration. If sterile API is claimed, the material must meet USP <71> or Ph. Eur. 2.6.1.

    For oral solutions and granules for reconstitution, the API is dissolved in purified water with sweeteners, preservatives, and buffers. The solution is protected from light if required, and pH stability data are generated in the intended container closure system. pH is controlled with Ph. Eur. 2.2.3, and density with Ph. Eur. 2.2.5. Microbial quality is controlled with USP <61> and USP <62> for non-sterile products, and preservative effectiveness is evaluated with USP <51> where preservatives are present.

    Dosage form Typical process route Critical API attributes Equipment or control method
    Tablet Direct compression or dry granulation Particle size distribution, bulk and tapped density, flow function coefficient, compactibility Rotary tablet press with force feeder; USP <1217>, USP <616>, USP <1174>
    Capsule Powder blending followed by dosator or tamping-pin fill Flow, density, segregation tendency, particle size distribution Capsule filler; USP <905>, USP <701>
    Granule High-shear or fluid-bed granulation, drying, milling Solubility, moisture sorption, binder compatibility, polymorph stability High-shear mixer, fluid-bed dryer; USP <711> after reconstitution
    Oral solution Dissolution in purified water, pH adjustment, filtration pH-dependent solubility, preservative compatibility, light sensitivity Ph. Eur. 2.2.3, 2.2.5, USP <51>
    Injectable Aseptic fill or terminal sterilisation Endotoxin, bioburden, particulate matter, pH stability, osmolality 0.22 µm sterilising-grade filter; USP <85>, USP <788>, Ph. Eur. 2.9.19

    When a Technical-Grade Supplier Is Compared with a Pharmacopoeial CEP-Grade Source

    Technical-grade lamivudine may be released against an internal specification that does not include pharmacopoeial related substances, residual solvents, elemental impurities, or chiral purity controls. Pharma grade API is released only after a full monograph and ICH Q3 panel is completed. Compared with emtricitabine, lamivudine differs in stereochemistry and substitution: both are cytidine analogues, but lamivudine is the (−)-enantiomer of 2′,3′-dideoxy-3′-thiacytidine, while emtricitabine is a fluorinated analogue. Compared with zidovudine, lamivudine has a different molecular structure and is not supplied as an azide-containing derivative; therefore azide-related residual testing is not part of the standard release panel. Compared with abacavir sulfate, lamivudine is not supplied as a sulfate salt and does not carry the same salt stoichiometry controls. The product also differs from research-grade or veterinary-grade material in packaging, documentation, regulatory status, and change management. Injectable grade differs from oral grade in bioburden, endotoxin, particulate, and packaging controls. The chiral purity of lamivudine is controlled because the pharmacopoeial monograph requires the (−)-enantiomer; the opposite enantiomer is controlled as a specified impurity by chiral HPLC or optical rotation. Non-pharmacopoeial lamivudine may not provide this chiral separation data, which can create downstream regulatory risk in finished dosage form filings.

    Storage and handling boundaries are defined by the manufacturer’s stability data. The API is stored in tightly closed containers protected from light, with controlled room temperature and humidity. If closure integrity is breached or moisture uptake is observed above the certified loss-on-drying limit, re-evaluation is required. The material should not be repackaged into unqualified containers because of potential particle size segregation and moisture ingress. Avoid prolonged exposure to strongly acidic or strongly alkaline media unless stability data support the intended process, because the cytidine analogue may undergo degradation under extreme pH conditions. For injectable operations, filtered solutions should be held for validated hold times only, as extended holding before sterilisation may increase bioburden and endotoxin risk beyond the qualified process envelope.

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