| HS Code | 120532 |
| Product Name | Lincomycin HCl Pharma Grade API |
| Api Name | Lincomycin Hydrochloride |
| Grade | Pharmaceutical Grade |
| Intended Dosage Forms | Tablet / Capsule / Granule / Injection |
| Routes Of Administration | Oral; Injectable |
| Therapeutic Category | Lincosamide antibiotic |
| Cas Number | 859-18-7 |
| Molecular Formula | C18H34N2O6S·HCl |
| Molecular Weight | 461.01 g/mol |
| Appearance | White or almost white crystalline powder |
| Solubility | Freely soluble in water; slightly soluble in alcohol; very slightly soluble in acetone |
| Assay Purity | ≥98% (HPLC, on dried basis) |
| Pharmacopoeial Compliance | USP/EP/CP |
| Storage Conditions | Store in a tightly closed container in a cool, dry place; protect from light, heat, and moisture |
| Shelf Life | 36 months when stored under recommended conditions |
As an accredited Lincomycin HCL 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 | Packaging: 25 kg net per sealed drum, double polyethylene-lined, for Lincomycin HCl Pharma Grade API, oral/injectable use. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized drums/cartons of Lincomycin HCL Pharma Grade API, secured, sealed, safely packed for transport. |
| Shipping | Lincomycin HCl Pharma Grade API ships in sealed, inert containers to preserve stability and purity. Store in a cool, dry environment away from light. All transportation follows cGMP and cold-chain guidelines when required, ensuring safe, compliant delivery for tablet, capsule, granule, and injectable manufacturing. |
| Storage | Store Lincomycin HCl Pharma Grade API in tightly sealed, original containers in a cool, dry, well-ventilated area, protected from light and moisture. Maintain controlled room temperature below 30°C. Keep away from incompatible substances and food. Ensure proper labeling and secure access. This preserves stability, potency, and suitability for tablet, capsule, granule, and injectable formulations. |
| Shelf Life | Shelf life is typically 24 months when stored in a cool, dry place, protected from light, in a tightly sealed container. |
For a high-dose oral tablet containing lincomycin hydrochloride monohydrate equivalent to 500 mg lincomycin base, the active constituent represents 56–67% w/w of the uncoated core when total core mass is held between 850 mg and 1000 mg. That high active fraction makes dry blending and direct compression flow-critical because lincomycin hydrochloride monohydrate is freely soluble in water and exhibits surface moisture uptake at relative humidity above 60% RH. Aqueous wet granulation is therefore selected when the downstream tablet needs a disintegration time below 15 min in purified water at 37 °C under USP <701> conditions. The process starts with high-shear granulation in a 300 L horizontal granulator at impeller speed 200–300 rpm and chopper speed 1500–3000 rpm; povidone K30 is dissolved in purified water at 5–8% w/w binder solution concentration and sprayed at 2–4% w/w dry binder content. Wet massing is limited to 3–6 min and the granules are discharged at a loss-on-drying of 1.5–2.5%, milled through a 1.0–1.5 mm screen, and dried in a fluid-bed dryer with inlet air at 60–70 °C and product temperature 35–45 °C to a final moisture specification of 1.0–2.5%. Tablet compression on a rotary press uses precompression 5–10 kN, main compression 15–25 kN, and target hardness 80–150 N. Crospovidone at 2–4% w/w and microcrystalline cellulose at 20–30% w/w are used to maintain tablet porosity; magnesium stearate is restricted to 0.5–1.5% w/w and blended for 3–5 min to avoid hydrophobic coating. Aqueous film coating with hydroxypropyl methylcellulose-based Opadry II is applied at 3–4% w/w weight gain with inlet temperature 65–75 °C, bed temperature 38–45 °C, and pan speed 6–10 rpm. Release testing follows USP <711> dissolution, USP <905> uniformity of dosage units, USP <921> water determination, and ICH Q3D elemental impurities; batch release also requires FDA 21 CFR 211.165 and 211.166 testing. The terminal finished dosage types are immediate-release film-coated tablets labeled at 250 mg or 500 mg lincomycin base.
| Component | Function | Proportion in uncoated core |
|---|---|---|
| Lincomycin hydrochloride monohydrate | Active pharmaceutical ingredient | 566.5 mg; 56–67% w/w |
| Microcrystalline cellulose | Filler/binder | 20–30% w/w |
| Partially pregelatinized starch | Filler | 10–20% w/w |
| Povidone K30 | Binder | 2–4% w/w |
| Crospovidone | Disintegrant | 2–4% w/w |
| Colloidal silicon dioxide | Glidant | 0.5–1.0% w/w |
| Magnesium stearate | Lubricant | 0.5–1.5% w/w |
| Opadry II coating | Film coat | 3–4% weight gain |
In capsule manufacturing, the 500 mg lincomycin base dose creates a dry blend with an active salt fraction of 70–81% w/w when the target fill weight is 700–800 mg per size 0 or 00 hard gelatin capsule. The active particle size distribution is controlled at 50–150 µm, because finer material increases cohesiveness and coarser material retards dissolution; the blend is not suitable for direct encapsulation without a granulation step because flow through a dosator nozzle becomes erratic at Carr’s index above 25%. A roller-compacted dry granulation route is therefore specified: the API is premixed with microcrystalline cellulose 10–20% w/w, lactose monohydrate 5–15% w/w, croscarmellose sodium 2–4% w/w, and colloidal silicon dioxide 0.3–0.8% w/w in a 600 L bin blender at 10 rpm for 20 min. The mixture is passed through a roller compactor at roll pressure 30–50 kN/cm, roll gap 2–4 mm, and roller speed 5–10 rpm; ribbons are milled through a 0.8–1.25 mm screen to produce granules with bulk density 0.55–0.65 g/mL and tapped density 0.70–0.80 g/mL. After lubrication with magnesium stearate 0.5–1.0% w/w for 3–5 min, the granules are filled on an intermittent-motion dosator encapsulator at 60,000–120,000 capsules/h. Because lincomycin hydrochloride monohydrate is hygroscopic, the granulation bay is maintained at 35–45% RH and the final granule moisture is controlled to 1.0–2.0% by Karl Fischer titration according to USP <921>. Release testing includes USP <711> dissolution with apparatus 2 paddle at 50 rpm, USP <905> content uniformity, USP <701> disintegration, ICH Q3C residual solvents, and 21 CFR 211.110 in-process control. The terminal finished dosage type is the hard gelatin capsule containing lincomycin hydrochloride monohydrate equivalent to 500 mg lincomycin base.
For sterile injectable solution, lincomycin hydrochloride monohydrate is dissolved in Water for Injection to achieve 300 mg/mL lincomycin base. Because the molecular weight of lincomycin hydrochloride monohydrate is 461.0 g/mol and lincomycin base is 406.5 g/mol, each litre of formulated solution contains 340.2 g of the monohydrate salt. The compounding vessel is 316L stainless steel with a chilled water jacket, and dissolution is performed at 15–25 °C with continuous recirculation through a 0.45 µm prefilter. The pH is adjusted with 1 M sodium hydroxide or hydrochloric acid to a target of 4.0–6.0, because acidic pH suppresses hydrolysis of the lincomycin amide bond and reduces related degradation products; the solution is held under nitrogen overlay with headspace oxygen maintained below 2% v/v. The solution is sterile-filtered through two 0.22 µm PVDF membrane filters in series, then aseptically filled into depyrogenated Type I borosilicate glass vials or ampoules under Grade A laminar airflow with Grade B background as required by EU GMP Annex 1 and FDA 21 CFR 211.113(b). Fill volume is controlled to 2 mL, 5 mL, 10 mL, or 20 mL; for multi-dose presentations, an antimicrobial preservative such as benzyl alcohol may be included at its pharmacopoeial permitted concentration, but only where regional licensing permits and only after preservative efficacy testing under USP <51>. Release testing includes USP <71> sterility, USP <85> bacterial endotoxins, USP <788> particulate matter in injections, USP <790> visible particulates, and ICH Q3D elemental impurities. Because published data for terminal sterilization of this specific lincomycin hydrochloride solution is limited, aseptic filtration remains the default route and thermal exposure must be validated before terminal sterilization is introduced. The terminal finished dosage types are sterile injectable solution vials, ampoules, and multi-dose vials labeled at 300 mg/mL lincomycin base equivalent.
Where national drug registers include lincomycin hydrochloride as a dry granule for oral suspension, the granule design is driven by the need to mask the intense bitterness of the API and to deliver a reconstituted concentration of 250 mg/5 mL lincomycin base. A representative 100 g granule batch containing 5.67 g lincomycin hydrochloride monohydrate would deliver 5.00 g lincomycin base after reconstitution to 100 mL, corresponding to 50 mg/mL or 250 mg/5 mL. The carrier system typically comprises sucrose or sorbitol at 70–85% w/w, xanthan gum 0.2–0.4% w/w, sodium carboxymethylcellulose 0.5–1.0% w/w, citric acid 0.1–0.3% w/w, sodium citrate 0.1–0.3% w/w, and a volatile mint or cherry flavor. The granulation process uses a hydroalcoholic binder solution containing povidone K30 at 2–4% w/w; wet mass is passed through a 1.0 mm screen, dried in a fluid-bed dryer at inlet 55–65 °C to final moisture below 1.5%, and sized through 16–40 mesh. The finished granules are packed into aluminum foil laminate sachets at 10 g, 20 g, or 100 g fill weights. Published compendial monographs for this specific lincomycin hydrochloride granule presentation are limited in several regions; therefore, release specifications are derived from the general monograph for oral powders and from ICH Q1A stability, ICH Q3B degradation products, and ICH Q3D elemental impurities, with USP <711> dissolution applied after reconstitution where justified. The terminal finished dosage types are single-dose or multi-dose sachets for reconstitution to an oral suspension.
In veterinary drinking-water formulations, lincomycin hydrochloride monohydrate is dry-blended with anhydrous citric acid, lactose monohydrate, and silica to produce a water-soluble powder with rapid dispersion. A typical 100 g sachet is formulated to contain 20–40 g lincomycin base equivalent, corresponding to 22.7–45.4 g lincomycin hydrochloride monohydrate; the product is administered through drinking water at a target concentration of 50–150 mg/L for growing pigs and poultry depending on the approved veterinary indication. Dry blending is performed in a 500 L ribbon blender at 20–30 rpm for 25–35 min; the mixture is deagglomerated through a 0.8 mm screen and filled into polyethylene-aluminum-foil laminate sachets under nitrogen. Dissolution performance is checked by adding a single sachet to 100 L of purified water at 20 °C, and complete dispersion must occur within 2 min without sedimentation; pH after dispersion is controlled to 3.5–5.5 to reduce hydrolysis of the lincomycin amide bond. Compliance for this non-sterile veterinary product is evaluated under Regulation (EU) 2019/6, ICH Q3C residual solvents, and ICH Q3D elemental impurities adapted under VICH guidance; in-process controls for blend uniformity and moisture follow 21 CFR 211.110. The terminal finished dosage types are water-soluble powder sachets for oral administration in drinking water for swine and poultry.
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Lincomycin Hydrochloride USP/Ph. Eur. pharmaceutical-grade active pharmaceutical ingredient, CAS 859-18-7, molecular formula C18H34N2O6S·HCl·H2O, molecular weight 461.01 g/mol, is a white or almost white crystalline powder supplied as the monohydrate salt for the manufacture of tablets, capsules, granules, oral solutions, and injectable dosage presentations. The product designation “Lincomycin HCL Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable” identifies a compendial-grade input rather than a single formulated product. Within this grade, manufacturers may assign subgrades according to post-crystallization processing: a direct-compression grade with controlled D90 and flow, a granulation grade with intermediate particle size, and an injection grade with tighter endotoxin and bioburden controls. The API is differentiated from technical-grade or feed-grade lincomycin hydrochloride by release testing under the current USP Lincomycin Hydrochloride monograph and the Ph. Eur. Lincomycin Hydrochloride monograph, residual solvent control under USP <467> Option A, elemental impurity control under ICH Q3D and USP <232>/<233>, and GMP execution under ICH Q7 and FDA 21 CFR 210/211. The monohydrate salt is freely soluble in water, which permits aqueous granulating fluids, oral liquid compounding, and parenteral concentrates at common processing concentrations without organic cosolvents. X-ray powder diffraction and infrared absorption against the pharmacopeial reference standard confirm crystalline identity; the salt is not interchangeable with lincomycin base or with clindamycin hydrochloride on a milligram basis because lincomycin HCl retains the 7(R)-hydroxy substituent, while clindamycin HCl is the 7(S)-chloro-7-deoxy derivative.
Compendial potency is calculated as micrograms of lincomycin base per milligram of dried substance; the established release interval is 790–815 µg/mg. This interval is not a performance claim but a pharmacopeial strength-and-purity band that prevents underdose and excess impurity loading. Related substance profiling by HPLC is executed with a system suitability resolution between lincomycin B and lincomycin A of not less than 1.5. Degradation in the solid state is most sensitive to free moisture; pharma-grade material is dried to a water content of 3.0–6.0% as the monohydrate and stored in tight containers at 20–25°C. Forced degradation studies following ICH Q1A and ICH Q1B demonstrate that the glycosidic linkage is vulnerable to acid-catalyzed hydrolysis when aqueous solutions are held below pH 2.0; published pH-rate data for this specific salt across all buffered parenteral vehicles is limited, so terminal sterilization and long-term solution stability must be established per formulation. Photostability testing under ICH Q1B is applied because bulk exposure to light may generate colored degradation products; the API is therefore packaged in light-resistant containers and protected during dispensing.
| Attribute | Release criterion | Method designation |
|---|---|---|
| Potency | 790–815 µg/mg dried basis | HPLC, USP monograph |
| Water | 3.0–6.0% | USP <921> Karl Fischer |
| pH of 5% aqueous solution | 3.0–5.5 | USP <791> |
| Specific rotation | +135° to +150° | USP <781> |
| Residual solvents | Conforms to USP <467> Option A | HS-GC |
| Elemental impurities | Conforms to ICH Q3D | ICP-MS per USP <233> |
| Bacterial endotoxins, injection grade | ≤0.50 EU/mg | USP <85> / Ph. Eur. 2.6.14 |
Chemical compliance alone does not control oral solid dosage processing. The same release panel is supplemented by powder-flow and particle-size testing for tablet, capsule, and granule applications, because a chemically compliant lot can still produce weight variation or lamination if crystal habit and fines are not constrained.
Lincomycin HCl is a high-dose antibiotic with tablet strengths commonly between 250 mg and 500 mg; formulations therefore contain a high fraction of API and are disproportionately influenced by API flow and compaction. Micronized powder with a D90 below 75 µm is suitable for wet granulation or capsule filling but can produce poor flow in direct compression; powder blend flow is quantified by Carr index and Hausner ratio according to USP <1174>, with direct compression blends generally requiring a Hausner ratio below 1.25. On a 16-station instrumented rotary tablet press at main compression force between 8 kN and 15 kN, blends containing high-fines lincomycin HCl display capping and lamination when the compaction pressure exceeds the brittle fracture threshold; the API’s needle-like crystal habit, when present, contributes to die-fill variation and sticking. Dry granulation by roller compaction is used to increase bulk density and reduce dust. The process is monitored by ribbon solid fraction and milled granule D50; overly compacted ribbons above solid fraction 0.75 generate hard granules with low compactability, while ribbons below 0.55 produce fines and may not resolve flow. A fluid-bed granulator with inlet air dew point below 6°C is used for aqueous top-spray granulation when a binder such as povidone or pregelatinized starch is applied; the exhaust temperature is held below 55°C to minimize hydrate loss and chemical degradation. Excipient incompatibility with lactose monohydrate should be assessed because lincomycin HCl contains secondary amine functionality; a related substance survey after accelerated storage at 40°C/75% RH is performed to detect Maillard-type adducts.
For immediate-release tablets and capsules, dissolution is evaluated according to USP <711>; a typical apparatus configuration uses USP Apparatus 2 at 50 rpm in 900 mL of 0.1 N hydrochloric acid, but the final method and Q value are product-specific. Uniformity of dosage units is confirmed by USP <905>. Capsule filling on a dosator-type machine with pin heights matched to bulk density is sensitive to granulate D90; granulate screened below 1.0 mm and conditioned to loss on drying below 2.0% reduces fill weight drift and dust adherence.
| Dosage route | Critical API attribute | Processing limit or equipment | Observed failure mode |
|---|---|---|---|
| Tablet | Hausner ratio | 1.20–1.35 after dry granulation; 16-station press | Capping, weight variation |
| Capsule | Granulate D90 | 250–500 µm after screening; dosator-type encapsulation | Fill weight drift, dust adherence |
| Granule | Loss on drying | ≤2.0% after fluid-bed drying; sieve 1.0 mm | Agglomeration, flow arrest |
| Injection | Bacterial endotoxins | ≤0.50 EU/mg; USP <85> | Depyrogenation failure |
Lincomycin HCl intended for injectable manufacturing is not supplied sterile, so the dosage form manufacturer must perform aseptic filtration, terminal sterilization where validated, or aseptic processing. The API grade for injection is controlled for bioburden and bacterial endotoxins; a release limit of ≤0.50 EU/mg is applied when the projected maximum adult daily dose yields an endotoxin load below 5 EU/kg body weight. Depyrogenation of API is not typically performed on the dry powder; instead, the formulation is dissolved and filtered through a 0.22 µm sterilizing membrane after dissolution. Holding time between dissolution and filtration is limited to 4 h at controlled room temperature to prevent microbial proliferation and pH drift. The solution pH is adjusted with hydrochloric acid or sodium hydroxide to 3.0–5.5. Terminal sterilization of aqueous solutions by autoclaving at 121°C is validated only if the solution remains within the degradation boundary; otherwise, aseptic filtration is required. Lyophilized formulations require cycle development based on vial heat transfer studies because published lyophilization cycle data for lincomycin HCl in specific diluent matrices is limited.
Particulate matter in the finished injectable product is evaluated according to USP <788>; for small-volume injections, the compendial limits are not more than 6000 particles per container ≥10 µm and not more than 600 particles per container ≥25 µm. Sterility testing of the finished injectable product follows USP <71> with membrane filtration and incubation at 20–25°C and 30–35°C for 14 days. The sulfur-containing glycosidic structure of lincomycin HCl is susceptible to oxidation; contact with strong oxidizing agents, peroxide residues, or permanganate cleaning residuals is controlled by HPLC related substance testing. Filter adsorption is assessed because lincomycin HCl at low concentration can bind to certain nylon membranes; polyethersulfone membranes are commonly evaluated with the solution pH adjusted to 3.0–5.5 before membrane selection is finalized.