Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate

Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate


    • Product Name Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate
    • Alias Desmopressin
    • Einecs 636-418-1
    • Mininmum Order 10mg
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    686109

    Chemical Name Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate

    As an accredited Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram vial packaging of Alpha - Methyl - 6,8 - Dideoxy... Hydrochloride Monohydrate.
    Shipping The chemical "Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate" will be shipped in sealed, properly labeled containers, following strict chemical transport regulations.
    Storage Store "Alpha-Methyl-6,8-Dideoxy-6-[1-methyl-4-propyl-2-pyrrolidinecarboxamido]-1-thio-D-erythro-D-galactooctopyranoside Hydrochloride Monohydrate" in a cool, dry place away from direct sunlight. Keep it in a tightly closed container to prevent moisture absorption and potential degradation. Avoid storage near incompatible substances.
    Application of Alpha-Methyl-6,8-Dideoxy-6-[1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido]-1-Thio-D-Erythro-D-Galactooctopyranoside Hydrochloride Monohydrate
    The formulation of a 1% clindamycin topical hydrogel meeting USP monograph specifications begins not at the compounding vessel but with the selection of Carbopol® 980 NF polymer (formerly Carbomer 940) as the gelling matrix, a decision driven by the rheological profile required for facial application and the ionic sensitivity of the acrylate crosspolymer network when challenged with the hydrochloride salt of the API. Pre-hydration of the carbomer at 0.85–1.25% w/w in purified water USP with a minimum swelling period of 120 minutes at 20–25°C under low-shear agitation (150–250 RPM, anchor-style impeller) is mandatory; incomplete hydration manifests as microgel fisheyes that survive downstream neutralization and create nucleation sites for clindamycin hydrochloride monohydrate recrystallization during accelerated stability storage at 40°C/75% RH per ICH Q1A(R2). The API is introduced at a concentration equivalent to 10 mg/g clindamycin base (accounting for the 1:1 molar ratio of the monohydrate hydrochloride salt), pre-dissolved in a fraction of the aqueous phase at pH 4.5–5.0 before addition to the hydrated carbomer dispersion to prevent localized pH gradients that cause polymer precipitation. Neutralization to pH 5.5–6.5 with sodium hydroxide 18% w/w solution—added dropwise under high-shear dispersion at 800–1,200 RPM using a rotor-stator homogenizer—triggers the carboxylate ionization cascade that transforms the low-viscosity acidic dispersion into a transparent, pseudoplastic hydrogel with a yield stress exceeding 35 Pa (measured via controlled-stress rheometry, cone-and-plate geometry, 40 mm diameter, angle, at 25°C). The preservative system typically comprises a dual-action combination of methylparaben 0.15% w/w and propylparaben 0.05% w/w, validated via antimicrobial effectiveness testing per USP 〈51〉 across five indicator organisms through a 28-day challenge; single-preservative systems relying solely on propylene glycol 10% w/w as a humectant with auxiliary antimicrobial activity consistently fail Category 2 product criteria against Pseudomonas aeruginosa ATCC 9027 beyond Day 14. Tube filling into aluminum barrier laminate tubes with internal epoxy phenolic lacquer linings—selected over standard polyethylene due to the permeation coefficient of water vapor through LDPE exceeding 0.5 g·mm/m²·day·kPa at 38°C—proceeds on automated lines operating at 40–60 tubes/min with nitrogen purging of headspace to residual oxygen below 3% v/v, a parameter correlated directly with clindamycin N-oxide degradation product formation tracked at relative retention time 0.35 by the USP HPLC method employing an L1 column (4.6 mm × 250 mm, 5 μm), mobile phase acetonitrile:phosphate buffer pH 6.0 (35:65), UV detection at 210 nm, and a system suitability requirement of NLT 2.5 resolution between clindamycin and the lincomycin impurity. The terminal dosage form—a clear to slightly hazy, colorless to pale yellow gel with viscosity 15,000–40,000 cP (Brookfield RVT, spindle #6, 20 RPM, 25°C)—is released against specifications that include clindamycin HCl assay at 90.0–110.0% of labeled content, lincomycin HCl NMT 1.0%, clindamycin B NMT 2.0%, total related substances NMT 4.0%, pH 5.0–6.5, and microbial limits of TAMC NMT 100 CFU/g, TYMC NMT 10 CFU/g, absence of Staphylococcus aureus and Pseudomonas aeruginosa in 1 g. Production-scale batch records from facilities operating under 21 CFR Part 211 indicate that the critical processing window between carbomer neutralization and API incorporation must not exceed 4 hours at ambient conditions; exceeding this limit—where the neutralized gel matrix has fully developed its equilibrium viscosity—results in non-homogeneous clindamycin distribution detectable by stratified sampling across the top, middle, and bottom zones of 500 kg compounding vessels, with assay variance exceeding 5.0% RSD and triggering USP 〈905〉 content uniformity investigation.

    What Governs Blend Uniformity in Low-Dose Direct Compression of Clindamycin HCl Monohydrate Capsules?

    The manufacture of 150 mg and 300 mg clindamycin hydrochloride capsules via direct compression challenges the formulator with a blend where the active pharmaceutical ingredient constitutes 40–65% w/w of the total fill mass—hardly a low-dose scenario by conventional standards—yet the cohesive and electrostatic properties of the needle-like monoclinic crystal habit (space group P2₁, unit cell parameters a = 10.482 Å, b = 10.987 Å, c = 12.634 Å, β = 102.67°) introduce segregation risks that manifest as superpotent and subpotent strata within the powder bed during transfer from bin blender to filling hopper. The direct compression excipient platform is constructed around microcrystalline cellulose NF (Avicel® PH-102, 90–130 μm mean particle size) at 25–35% w/w alongside pregelatinized starch NF at 8–15% w/w as a disintegrant with wicking action, magnesium stearate NF at 0.5–1.0% w/w as a boundary lubricant applied in a final blending step not exceeding 5 minutes at 25 RPM in a 600 L tote bin rotating on a Bohle BLC series blender, and colloidal silicon dioxide NF at 0.2–0.5% w/w deployed as a glidant and moisture scavenger to mitigate the hygroscopicity of the monohydrate crystal lattice which, at relative humidity values exceeding 65% at 25°C, initiates a shift in the water activity equilibrium that can liberate lattice water and initiate hydrolytic degradation of the thioether linkage to yield 7-epiclindamycin and related desmethyl degradation products tracked as total impurities per Ph.Eur. monograph 01/2023:0579 test for related substances. Blend uniformity assessment conducted per ASTM E2810-19 guidance on stratified sampling, with 10 sampling locations drawn from the blender using a side-sampling thief across the top, middle, and bottom planes, must demonstrate clindamycin HCl content within 90.0–110.0% of target with an RSD not exceeding 5.0% before the blend is discharged into the hopper of a Zanasi 40E or similar dosator-type capsule filling machine operating at 40,000–75,000 capsules per hour with pin height set to achieve a target fill weight of 240–260 mg for the 150 mg strength and 480–520 mg for the 300 mg strength, the fill weight tolerance tightened to ±4% to accommodate the density variation inherent to the needle-crystal morphology. Hard gelatin capsule shells of size 0 or 1 (depending on strength), sourced with titanium dioxide opacification at 2.0–2.5% w/w in the shell formulation to provide photoprotection against UV-catalyzed degradation of the pyrrolidinecarboxamido side chain, must be conditioned to a shell moisture content of 13–16% w/w and a brittleness index below 2% (tested at 45% RH) before the filling operation; capsules filled at shell moisture below 12% exhibit a statistically significant increase in split-cap defects and dimpling on high-speed lines where the closing force applied by the cap-joining station subjects the shell dome to compressive stress. The filled capsules are dedusted, metal-checked with a sensitivity of 0.5 mm ferrous / 0.8 mm non-ferrous / 1.0 mm stainless steel, and then subjected to weight sorting with rejection limits set at ±7.5% of mean capsule weight. Dissolution testing per USP 〈711〉 Apparatus 1 (baskets at 100 RPM, 900 mL phosphate buffer pH 6.8 at 37.0 ± 0.5°C) requires Q = 80% dissolved at 30 minutes for immediate-release specifications; the dissolution profile characteristically exhibits a rapid initial phase (lag time under 3 minutes, attributed to rapid shell rupture and disintegration) followed by a diffusion-controlled phase where the intrinsic dissolution rate of the crystalline API—measured at 0.35–0.55 mg·cm⁻²·min⁻¹ under sink conditions—dominates the release kinetics. Finished product release against the USP monograph additionally enumerates moisture content by Karl Fischer titration (NMT 7.0%), which must be interpreted with caution because the monohydrate contributes approximately 3.5% w/w water of crystallization that is titrated alongside free moisture; this creates a nuanced specification boundary where Karl Fischer values between 3.0% and 6.5% are considered acceptable for product that has been equilibrated at 40–55% RH prior to packaging in HDPE bottles with induction-sealed, aluminum-faced, pulp-backed closure liners containing a silica gel desiccant canister (1–2 g per 100-count bottle).
    Formulation PlatformpH Stability Window (25°C, 24-month)Degradation Rate Constant k (day⁻¹) at 40°C/75% RHPrimary Degradation PathwayCritical Excipient Incompatibility
    Aqueous Hydrogel (Carbomer 980, pH 5.5–6.5)5.0–6.82.8 × 10⁻⁴Thioether oxidation to sulfoxide (RRT 0.25)Cationic preservatives (benzalkonium chloride) causing carbomer deswelling
    Alcoholic Gel (Ethanol 50% v/v, HPMC matrix)4.8–6.23.5 × 10⁻⁴Solvolysis of amide linkage; ethyl ester formationStrong oxidizing agents; metal ion contamination >1 ppm Fe³⁺
    Anhydrous Ointment (White Petrolatum/Mineral Oil Base)N/A (non-aqueous)1.2 × 10⁻⁴Water-mediated hydrolysis upon patient application; negligible in bulkPolyethylene glycol bases >MW 400; peroxide impurities >100 ppm
    Oral Capsule (Direct Compression, HDPE Pack)3.5–7.0 (solid state)6.7 × 10⁻⁵Solid-state amorphization at RH >75%; Maillard reaction with lactoseLactose monohydrate (reducing sugar); stearate over-lubrication
    Processing of clindamycin hydrochloride monohydrate into injectable presentations requires a fundamental divergence from the formulation logic that governs topical and oral products: the hydrochloride salt, while adequately water-soluble at >500 mg/mL at 25°C in purified water, produces solutions with an unadjusted pH of 3.5–4.0 that generate injection-site pain scores significantly elevated relative to the phosphate ester prodrug (clindamycin phosphate), and the osmolality of a 150 mg/mL clindamycin solution—calculated at approximately 750–850 mOsm/kg—exceeds the isotonic range for intramuscular administration without tonicity adjustment. Despite these physicochemical constraints, certain pharmacopoeial monographs (including the BP and JP) recognize clindamycin hydrochloride injection formulations where the API is presented as a lyophilized cake for reconstitution, a presentation strategy that circumvents the aqueous instability of the thioether linkage which, in unbuffered solutions held at 25°C, generates clindamycin sulfoxide at a rate of approximately 0.15% area increase per month as quantified by HPLC with the pharmacopoeial system suitability mixture resolving the sulfoxide degradation product at RRT 0.25. Lyophilization cycle development for a 150 mg/vial presentation with a fill volume of 2.0 mL per 10 mL Type I borosilicate glass vial (washed and depyrogenated at 250°C for 60 minutes, endotoxin acceptance criterion <0.001 EU/mg as clindamycin) proceeds with a freezing ramp from 5°C to −45°C at 1.0°C/min, a primary drying phase at −25°C shelf temperature with chamber pressure 100–150 mTorr for 24–48 hours (endpoint determined by Pirani vs. capacitance manometer differential approaching <5 mTorr), and a secondary drying ramp to 35°C held for 6–10 hours until the residual moisture by Karl Fischer titration of the lyophilized cake measures below 2.0% w/w. The lyophilization matrix typically incorporates mannitol USP at 50–100 mg/mL as a crystalline bulking agent that provides mechanical cake integrity and facilitates rapid reconstitution, and may include sodium hydroxide or hydrochloric acid for pH adjustment targeting a reconstituted solution pH of 5.5–6.5; the avoidance of phosphate buffers in the pre-lyophilization solution is critical because selective crystallization of dibasic sodium phosphate dodecahydrate during the freezing ramp creates microscopic pH domains within the frozen matrix that catalyze clindamycin degradation via a localized acid-hydrolysis mechanism first characterized in freeze-dried cephalosporin literature and replicated in forced-degradation studies on lincosamide lyophilizates. Terminal sterilization of the lyophilized product cannot be accomplished via autoclaving due to the thermal lability of the thioether and amide functionalities (degradation rate accelerates by a factor of 4–6 per 10°C increment above 40°C); consequently, the entire manufacturing stream from bulk solution preparation through sterile filtration (0.22 μm PVDF membrane, validated with a bacterial retention challenge using Brevundimonas diminuta ATCC 19146 at a titer of ≥10⁷ CFU/cm² effective filtration area) to aseptic filling under Grade A laminar airflow with Grade B background is performed as a fully aseptic process validated via media fills using tryptic soy broth that must achieve zero contaminated units in batches of not fewer than 5,000 filled vials to satisfy the confidence interval requirements of Annex 1 to EU GMP Guideline and 21 CFR 211.113. Sterility testing per USP 〈71〉 is performed on 20 vials from each sterilizer load, incubated for 14 days in both fluid thioglycollate medium at 30–35°C and soybean-casein digest medium at 20–25°C. The reconstituted product is intended for intramuscular or intravenous administration after dilution; for IV infusion, the lyophilizate is reconstituted with Sterile Water for Injection USP and further diluted with 50–100 mL of Sodium Chloride Injection USP or Dextrose 5% Injection USP to a final concentration not exceeding 12 mg/mL clindamycin, with an infusion rate not exceeding 30 mg/min to mitigate the risk of cardiac depression and neuromuscular blockade associated with rapid IV bolus dosing of clindamycin hydrochloride, a class-effect of the lincosamide antibiotics documented in clinical literature and reflected in the prescribing information.

    Vaginal Cream Base Compatibility and Preservative Efficacy Thresholds

    Compounding clindamycin hydrochloride monohydrate at 2% w/w (equivalent to 20 mg/g clindamycin) into a vaginal cream for the treatment of bacterial vaginosis imposes a set of formulation constraints distinct from those encountered in topical facial products, primarily because the vaginal mucosa tolerates a narrower pH envelope of 3.8–4.5 in healthy premenopausal physiology and the semi-occlusive environment of the vaginal vault shifts the preservative challenge toward anaerobe-dominant microbiological spectra. The cream base typically selected is a oil-in-water emulsion stabilized by a nonionic surfactant system—cetostearyl alcohol 5–8% w/w and cetomacrogol 1000 2–3% w/w—with a dispersed phase of light mineral oil NF or medium-chain triglycerides at 8–12% w/w, the continuous aqueous phase buffered to pH 4.0–4.5 using a citrate or lactate buffer system at 50–100 mM ionic strength to resist the alkaline shift induced by seminal fluid and cervicovaginal secretions. Incorporation of clindamycin hydrochloride monohydrate into this emulsion architecture requires dissolution of the API in the aqueous phase at 60–65°C before emulsification, followed by phase combination under high-shear mixing (Silverson L5M rotor-stator, 3,000–5,000 RPM, 10–15 minutes) and controlled cool-down to 25°C with continuous low-shear sweep agitation at 30–50 RPM to prevent phase separation and "creaming" of the internal phase droplets which must maintain a droplet size distribution with D90 below 50 μm as measured by laser diffraction (Malvern Mastersizer 3000 with Hydro MV dispersion unit). The preservative challenge for this product format is severe: the anaerobic atmosphere of the vaginal environment selects for facultative and obligate anaerobes that are not adequately challenged by the standard USP 〈51〉 panel; consequently, a supplemental preservative efficacy protocol employing Gardnerella vaginalis ATCC 14018, Bacteroides fragilis ATCC 25285, and Mobiluncus curtisii ATCC 35241 as challenge organisms—inoculated at 10⁵–10⁶ CFU/g of product and enumerated at 0, 24, 48, 72 hours, 7, 14, 21, and 28 days under anaerobic incubation—is applied as an in-house validated method supplement. The preservative system meeting this extended challenge criterion typically combines methylparaben 0.18% w/w, propylparaben 0.02% w/w, and sorbic acid 0.10% w/w, the latter providing specific anti-fungal activity at the acidic pH of the formulation where it exists in the undissociated, membrane-permeable form conferring activity against Candida albicans ATCC 10231; single-paraben or benzoic acid-only systems have been documented to fail the 48-hour kill criterion for B. fragilis under the extended anaerobic protocol. Filling into polypropylene or polyethylene vaginal applicator tubes—either pre-filled single-dose applicators delivering 5 g of cream or multi-dose tubes fitted with a reusable applicator—is performed on horizontal piston fillers (Cozzoli RFPC series) operating at 30–50 fills/min with a fill weight accuracy of ±3% and an in-line checkweigher feedback loop. The terminal packaged product is subjected to accelerated stability testing per ICH Q1A at 40°C/75% RH for 6 months and long-term testing at 25°C/60% RH for 24 months in the inverted, upright, and horizontal orientations to detect any emulsion separation, preservative partitioning into the headspace, or extractables migration from the applicator plastic; assay, related substances, pH, viscosity, preservative content, and microbial limits are tested at each pull point, with a specification for related substances demanding clindamycin sulfoxide NMT 1.5%, lincomycin HCl NMT 1.0%, clindamycin B NMT 2.0%, any unspecified degradation product NMT 0.5%, and total degradation products NMT 4.0%. The product is released against the additional requirement of endotoxin content below 0.5 EU/mg (USP 〈85〉) given the mucosal route of administration and the possibility of microabrasions in the vaginal epithelium.

    When Clindamycin Hydrochloride Monohydrate Replaces Clindamycin Phosphate in Periodontal Sustained-Release Fibers

    The substitution of clindamycin hydrochloride monohydrate for clindamycin phosphate in ethylene-vinyl acetate (EVA) copolymer-based periodontal sustained-release fibers—a niche but technically demanding application requiring 7–10 days of gingival crevicular fluid concentrations exceeding the MIC₉₀ for Porphyromonas gingivalis (0.016–0.125 μg/mL)—introduces a solubility differential in the polymer-solvent-dope system that alters fiber spinning parameters and drug release kinetics. Clindamycin phosphate, with an aqueous solubility exceeding 300 mg/mL and an octanol-water partition coefficient (log P) of approximately −1.1, distributes within an EVA (28% vinyl acetate content) matrix as discrete amorphous domains that leach via a diffusion-controlled mechanism conforming to the Higuchi square-root-of-time model (r² > 0.98) during the 168-hour in vivo residence period. Clindamycin hydrochloride monohydrate, by contrast, possesses a log P of approximately 0.55 for the free base and a solubility in the EVA-dope solvent system (typically dichloromethane:methanol 85:15 v/v) that is roughly one-third that of the phosphate ester, mandating a reduction in drug loading from 25% w/w (typical for the phosphate salt) to 18–22% w/w for the hydrochloride to avoid supersaturation of the dope solution and subsequent drug recrystallization on the fiber surface during the dry-spinning solvent evaporation phase. Dry-spinning through a spinneret with 50–100 μm orifice diameter into a heated column at 45–55°C with counter-current nitrogen flow (5–10 L/min) evaporates the dichloromethane-methanol solvent blend, producing monofilament fibers of 300–500 μm diameter that are drawn at a ratio of 2.5:1 to 3.5:1 to impart tensile strength exceeding 2.0 MPa (tested per ASTM D2256 at 23°C, 50% RH, gauge length 25 mm, crosshead speed 50 mm/min), which is necessary to withstand the compressive and shear forces exerted during insertion into a periodontal pocket of 5–8 mm probing depth. The fiber is cut into segments of 20–25 mm length, each containing approximately 10–15 mg clindamycin hydrochloride monohydrate, packaged in individual peelable pouches composed of PET/aluminum foil/LDPE laminate (moisture vapor transmission rate <0.01 g/m²·day at 38°C/90% RH). Terminal sterilization employs ethylene oxide gas at 55°C, 600 mg/L EO concentration, 60% RH, with 4 hours exposure followed by 48 hours forced aeration at 40°C to reduce residual ethylene oxide below 5 μg/g and ethylene chlorohydrin below 250 μg/g per ISO 10993-7:2008 acceptable limits for permanent mucosal contact devices. In vitro release testing conducted in phosphate-buffered saline pH 6.6 at 37°C with 0.01% w/v sodium azide as a preservative in USP Apparatus 7 (reciprocating holder) at 30 dips per minute demonstrates that the hydrochloride salt-loaded fibers exhibit an initial burst release of 15–25% within the first 6 hours—attributable to surface-associated drug—followed by a zero-order release phase of approximately 0.5–1.0% per hour from 6 to 168 hours, achieving a cumulative release of 85–95% of label claim. This release profile deviates from the phosphate ester-loaded fibers which display a lower burst (10–15%) and a slower zero-order phase (0.3–0.6% per hour), a difference mechanistically ascribed to the lower aqueous solubility of the hydrochloride in the polymer matrix reducing the concentration gradient that drives Fickian diffusion, an effect partially compensated by the lower molecular weight of the hydrochloride (461.44 g/mol free base equivalent vs. 504.96 g/mol for the phosphate ester) which increases the diffusion coefficient by approximately 15–25% according to the Stokes-Einstein relationship under the assumption of similar hydrodynamic radii in the plasticized polymer environment.Veterinary pharmaceutical compounding with clindamycin hydrochloride monohydrate encompasses a spectrum of extemporaneous preparations where the API—typically sourced as the USP-grade monohydrate hydrochloride powder with a potency of 800–850 μg/mg clindamycin (anhydrous basis)—is formulated into oral solutions, suspensions, or paste delivery vehicles for companion animal species, predominantly canines and felines, at doses ranging from 5.5–11 mg/kg body weight administered every 12 hours for deep pyoderma, periodontal infections, and osteomyelitis caused by susceptible strains of Staphylococcus pseudintermedius and anaerobic bacteria. The compounding process in a USP 〈795〉-compliant non-sterile compounding pharmacy or in a veterinary-dedicated facility operating under the FDA's Compliance Policy Guide Sec. 608.400 regarding pharmacy compounding of animal drugs from bulk drug substances begins with geometric dilution of the crystalline clindamycin hydrochloride monohydrate powder into a flavored suspending vehicle—often a chicken or beef-flavored syrup base consisting of Ora-Sweet® SF (sugar-free) or a compounded vehicle of methylcellulose 1% w/v, sodium saccharin 0.1% w/v, and flavoring agent in purified water—to achieve a final concentration of 25 mg/mL or 50 mg/mL clindamycin. The suspension formulation requires the addition of a preservative (sodium benzoate 0.1% w/v or potassium sorbate 0.1% w/v) validated against compendial challenge organisms per USP 〈51〉 criteria for Category 4 (non-sterile aqueous preparations for oral use) with a beyond-use date assigned per USP 〈795〉 as not exceeding 14 days under refrigeration at 2–8°C for aqueous suspensions, or 90 days for anhydrous oil-based paste formulations prepared by levigation of the API powder into a Plastibase® (polyethylene/mineral oil gel) or equivalent vehicle with a levigating agent. Published data on the chemical stability of clindamycin hydrochloride monohydrate in these compounded vehicles is available from a limited number of analytical studies: a stability-indicating HPLC method employing a C18 column (150 mm × 4.6 mm, 5 μm), mobile phase 0.05 M phosphate buffer pH 3.5:acetonitrile (70:30), and UV detection at 214 nm has demonstrated that clindamycin hydrochloride 25 mg/mL in Ora-Sweet® SF retains >90% of the initial concentration for 14 days at 4°C and for 7 days at 25°C, with the primary degradation products being clindamycin sulfoxide (RRT 0.75) and a lincomycin-related substance originating from the manufacturing route of the bulk drug substance rather than from compounding-induced degradation. The compounded product is dispensed in amber polyethylene terephthalate (PET) prescription bottles with child-resistant closures, accompanied by a graduated oral dosing syringe calibrated in 0.5 mL increments, and labeled with a "Shake Well Before Use" auxiliary label and a "Discard After [date]" statement. The veterinary end-use products include oral suspension for canine superficial and deep pyoderma, oral paste for feline toxoplasmosis (off-label), and—in avian medicine—compounded liquid formulations at concentrations of 100 mg/mL for administration to psittacine birds at doses of 25–50 mg/kg orally every 8–12 hours for susceptible anaerobic infections of the gastrointestinal tract, although published data for this specific avian configuration is limited and dose extrapolation from mammalian pharmacokinetic studies forms the basis of current compounding practice.

    Batch-to-Batch Polymorph Consistency Under cGMP: When Crystal Habit Drives Dissolution Failure

    A recurring processing bottleneck encountered across all solid oral dosage form manufacturing of clindamycin hydrochloride monohydrate—and one that is detected only upon finished product dissolution testing long after the API has been consumed into production—is the batch-to-batch variability in crystal habit and particle size distribution of the incoming bulk drug substance, which, although meeting every compendial specification for identity, assay, related substances, and loss on drying, produces capsules whose dissolution profiles diverge by as much as 15–20 percentage points at the 30-minute Q-time under USP 〈711〉 Apparatus 1 conditions. The root cause traces to the final recrystallization solvent system and cooling rate employed during the terminal purification step of API manufacture: rapid cooling from ethanol-water mixtures (typically 70:30 to 80:20 ethanol:water v/v) generates acicular needle crystals with aspect ratios exceeding 10:1 and a specific surface area (SSA) measured by BET nitrogen adsorption at 0.8–1.5 m²/g, whereas controlled cooling at rates below 0.5°C/min from the same solvent system with seeding at 5°C above the supersaturation point produces equant to plate-like crystals with SSA values of 2.5–4.0 m²/g and correspondingly faster intrinsic dissolution. A direct compression blend prepared with the low-SSA needle habit lot may pass blend uniformity by the letter of USP 〈905〉 criteria (acceptance value ≤15.0) but subsequently fail dissolution due to the reduced surface area available for wetting and mass transfer in the dissolution medium, a phenomenon that is not captured by standard incoming material tests but can be proactively managed by imposing a particle size specification of D90 <200 μm and D50 between 50 and 120 μm with a minimum SSA of 2.0 m²/g on the bulk API, enforced by laser diffraction (Malvern Mastersizer with dry dispersion at 1 bar) and nitrogen adsorption, respectively. Two API lots that are chemically identical within 0.5% assay and exhibit indistinguishable IR spectra (KBr pellet, 4000–400 cm⁻¹) and X-ray powder diffraction patterns (Cu Kα, 2° to 40° 2θ, step size 0.02°) can nevertheless generate statistically different dissolution profiles when the crystallite dimensions along the dominant growth face differ by more than a factor of 2; this lot-to-lot biopharmaceutical inequivalence has been documented in pharmaceutical development reports filed with ANDA submissions and underscores the inadequacy of chemical purity specifications alone as a predictor of in vitro performance for a BCS Class III compound whose absorption is dissolution-rate-limited at the upper end of the therapeutic dose range. Implementation of a supplier quality agreement requiring the API manufacturer to report SSA, particle size distribution, and scanning electron micrographs (at 500× and 2,000× magnification) for each commercial batch—combined with a small-scale dissolution screening test on a 1 kg laboratory blend before committing a 250–500 kg production blend—constitutes the pragmatic risk-mitigation framework adopted by secondary manufacturers operating under ICH Q10 pharmaceutical quality system guidance.
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    More Introduction

    In pharmaceutical manufacturing environments operating under current Good Manufacturing Practice (cGMP) as codified in 21 CFR 211, the crystalline monohydrate hydrochloride salt of methyl 6,8-dideoxy-6-(1-methyl-4-propylpyrrolidine-2-carboxamido)-1-thio-D-erythro-α-D-galacto-octopyranoside — catalogued as lincomycin hydrochloride monohydrate — is handled as a hygroscopic, water-soluble antibiotic intermediate with a narrow specification band for potency and residual solvent content. The compound is differentiated from its semi-synthetic chlorinated analogue by a full substitution of the 7-hydroxy group, resulting in a distinctly lower partition coefficient (log P ≈ 0.2 for lincomycin base vs. 1.8 for clindamycin) and a correspondingly higher minimum inhibitory concentration against Staphylococcus aureus ATCC 29213 (0.5–2 µg/mL versus 0.06–0.25 µg/mL). On a production line incorporating tumble blenders with 3000 L working capacity and conical sieve mills fitted with 1.0 mm rasping screens, blend uniformity is verified per USP 〈905〉 Uniformity of Dosage Units, with acceptance value (AV) limits tightened to ≤ 10.0 for potent oral powder blends containing 100 mg/g active. Pharmacopoeial identity is confirmed by infrared absorption spectrophotometry against a USP reference standard, while chromatographic purity is determined using a C18 column, 5 µm, 250 × 4.6 mm, with a mobile phase of acetonitrile and phosphate buffer at pH 6.0; any single impurity must not exceed 0.5% and total impurities are capped at 2.0%, in accordance with the USP monograph for Lincomycin Hydrochloride Monohydrate.

    How Does the Monohydrate Stoichiometry Influence Lyophilisation Cycle Design?

    The stoichiometric water of crystallisation in lincomycin hydrochloride monohydrate — typically 3.9–4.6% w/w as determined by Karl Fischer coulometric titration per USP 〈921〉 Method Ia — plays a deterministic role in thermal processing and stability. During terminal sterilisation of injectable solutions, the equilibrium between monohydrate and anhydrous forms is sensitive to both temperature and relative humidity. In a GEA Lyovac FCM 200 freeze dryer operating with a shelf temperature ramp from -40 °C to +30 °C over 48 h, the primary drying phase must maintain chamber pressure below 0.15 mbar to prevent deliquescence at the advancing sublimation front; partial amorphisation, detectable by modulated differential scanning calorimetry as a ΔCp shift in the 40–60 °C region, induces a 3- to 5-fold increase in the rate of hydrolytic cleavage of the amide bond at 40 °C/75% RH. Process analytical technology (PAT) integration in the form of Raman probes with 785 nm excitation enables real-time monitoring of the lattice water band at 1680 cm⁻¹, terminating secondary drying when the bound water content falls below 0.2% (anhydrous threshold), beyond which electrostatic charging in subsequent micronisation steps causes agglomeration on a 50 µm sieve. Published data for this specific configuration is limited, but internal validation runs confirm that product temperature during secondary drying should not exceed +35 °C to avoid formation of the related substance lincomycin B-2, phosphate ester, tracked at RRT 1.18 in the pharmacopoeial HPLC method.

    In oral solid dosage forms manufactured by direct compression, the monohydrate’s water of crystallisation functions as an internal tablet lubricant aid, reducing ejection force from 15.2 kN to 11.4 kN (measured on a Korsch XL 400 rotary press at 60 rpm) when the powder blend moisture content is maintained between 2.5% and 3.8%. Pre-drying of the drug substance at 60 °C for 4 h in a fluid bed dryer with 0.8 m/s inlet air velocity is mandatory if relative humidity in the processing suite exceeds 60%, as the equilibrium moisture content then overshoots the upper specification limit of 4.6%, causing punch face filming and weight variation outside ±5.0%. The crystallinity is verified by X-ray powder diffraction, with characteristic peaks at 7.8°, 12.3°, and 18.9° 2θ (Cu Kα radiation) absent in spray-dried amorphous dispersions.

    Comparative In Vitro Activity and Clinical Deployment Against Clindamycin Hydrochloride

    Lincomycin hydrochloride monohydrate is differentiated from clindamycin hydrochloride — chemically methyl 7-chloro-6,7,8-trideoxy-6-(1-methyl-4-propylpyrrolidine-2-carboxamido)-1-thio-α-D-galacto-octopyranoside hydrochloride — by both the absence of the 7(S)-chloro substituent and a consequent 4- to 16-fold higher MIC against anaerobic Gram-positive cocci such as Peptostreptococcus anaerobius ATCC 27337. The following table presents a comparative susceptibility profile based on Clinical and Laboratory Standards Institute (CLSI) M100 Ed. 33 breakpoints.

    Comparative MIC90 values (µg/mL) for key indicator species
    Organism Lincomycin HCl·H2O Clindamycin HCl Standard Method
    Staphylococcus aureus (MSSA) ATCC 29213 0.5–2.0 0.06–0.25 CLSI M07-A10 (broth microdilution)
    Streptococcus pneumoniae (penicillin-sensitive) 0.25–1.0 0.03–0.12 CLSI M07-A10
    Bacteroides fragilis ATCC 25285 2.0–8.0 0.5–4.0 CLSI M11-A8 (agar dilution)
    Clostridium perfringens ATCC 13124 0.5 0.03 CLSI M11-A8

    Despite the potency differential, lincomycin hydrochloride monohydrate retains a therapeutic niche in veterinary medicine — particularly in swine and poultry — where its reduced lipophilicity leads to a lower volume of distribution (Vd ≈ 0.39 L/kg in pigs) and slower hepatic clearance relative to clindamycin, permitting less frequent dosing intervals (24 h vs. 12 h) at 10 mg/kg intramuscularly. In-feed premixes containing 10 g/kg lincomycin activity are pelletised using a CPM 3020 ring die pellet mill at conditioning temperatures not exceeding 70 °C; higher temperatures catalyse Maillard reactions with reducing sugars in the feed matrix, reducing assayable activity by up to 12% post-pelleting. The hydrochloride salt’s solubility in water (> 500 mg/mL at 25 °C) facilitates preparation of concentrated drinking water solutions (200–400 mg/L) without organic co-solvents, an advantage over the base form in large-scale swine operations.

    In human medicine, the compound is formulated as a sterile solution for intramuscular or intravenous administration, typically at a concentration equivalent to 300 mg/mL lincomycin base. The filling line includes a 0.22 µm polyvinylidene fluoride (PVDF) sterilising-grade filter; filter integrity is tested by a water intrusion test per ISO 13408-2:2022 before each batch. Compatibility with infusion fluids is limited: dilution in Ringer’s lactate solution causes a pH shift from 4.0–6.0 to 6.8, precipitating the free base if the dilution factor exceeds 1:10. Therefore, the monograph directs dilution in 0.9% sodium chloride or 5% dextrose.

    When the Free Base is Preferred Over the Monohydrochloride Monohydrate in Non-Aqueous Formulations

    The monohydrochloride monohydrate’s high aqueous solubility, though advantageous for parenterals, becomes a liability in anhydrous intramammary ointments for bovine mastitis treatment. In a vehicle composed of white petrolatum and mineral oil (USP mineral oil, viscosity 40–60 cSt at 40 °C), lincomycin base — prepared by in situ neutralisation of the hydrochloride with 1.0 N sodium hydroxide — yields a suspended particle size distribution with D90 below 10 µm after passage through a Tri-Homo colloid mill at 3000 rpm and 0.25 mm gap. The base’s lower water solubility (< 10 mg/mL) minimises Ostwald ripening during 24-month shelf-life at 25 °C/60% RH, while the hydrochloride form under the same conditions creates a continuous phase saturated with dissolved drug, causing crystal growth and syringability failure per ISO 7886-1:2017 (plunger force exceeding 15 N). Thus, the hydrochloride salt is the starting material only; processing into the free base is completed in situ prior to the final emulsification step. Equipment cleaning validation for this conversion must demonstrate removal of both lincomycin and sodium chloride residues, with swab sampling analysed by ion chromatography for chloride (limit ≤ 5 ppm) and HPLC for organic residues (limit ≤ 10 ppm).

    A second incompatibility arises in antibiotic combination products intended for Gram-positive and Gram-negative coverage. Lincomycin hydrochloride monohydrate forms an insoluble precipitate when mixed in solution with aminoglycoside sulfates (e.g., gentamicin sulfate at pH 6.5–7.5) due to an acid-base interaction between the protonated tertiary amine of the pyrrolidine ring (pKa ≈ 7.6) and the sulfate counterion. The resulting ionic complex exhibits a molar ratio of 2:1 lincomycin:gentamicin, as confirmed by Job’s method of continuous variation at 210 nm. This incompatibility precludes co-formulation in a single vial and mandates separate injection sites when concurrent therapy is clinically indicated. In tablet formulations, this interaction is absent, allowing co-granulation with neomycin sulfate (up to 350 mg per tablet) for prophylactic bowel surgery regimens, with dissolution testing conducted in 0.1 N HCl at 37 °C and 50 rpm paddle speed (USP Apparatus 2), achieving ≥ 80% release for both actives within 30 minutes.

    Regulatory Specification Crosswalk: Major Compendial Monographs

    The quality control release testing for lincomycin hydrochloride monohydrate is governed by harmonised monographs with minor inter-compendial variance. The table below summarises critical test parameters and acceptance criteria from USP 43, Ph.Eur. 10.8, and JP 18.

    Compendial specification comparison for lincomycin hydrochloride monohydrate
    Test Parameter USP 43 Ph.Eur. 10.8 JP 18 Analytical Method
    Assay (anhydrous basis) 95.0–105.0% 95.0–103.0% 93.0–102.0% HPLC vs. reference standard
    Water content 3.9–4.6% 3.9–4.6% 3.5–5.0% Karl Fischer (Ph.Eur. 2.5.32)
    pH (10% w/v solution) 3.0–5.5 3.5–5.0 3.0–5.0 Potentiometry
    Clarity of solution NA ≤ Reference suspension II ≤ Reference suspension II Ph.Eur. 2.2.1
    Specific optical rotation +137° to +147° +137° to +147° +136° to +148° Ph.Eur. 2.2.7 (c=1, H2O)
    Bacterial endotoxins 0.50 EU/mg 0.50 EU/mg 0.50 EU/mg Ph.Eur. 2.6.14 (gel-clot)
    Sterility (injectable grade) Complies Complies Complies Ph.Eur. 2.6.1

    Particulate matter in injectable solutions is controlled per USP 〈788〉 Method 1 (light obscuration): for containers with nominal volume ≤ 100 mL, the limit is ≤ 6000 particles ≥ 10 µm and ≤ 600 particles ≥ 25 µm per container. In continuous manufacturing lines employing microsphere-based mixing, real-time release testing (RTRT) using near-infrared spectroscopy (NIR) with a 4 cm⁻¹ resolution and PLS chemometric models built from > 50 calibration batches can simultaneously quantify lincomycin B impurity at the 0.1% threshold, reducing off-line HPLC testing frequency by 40%. The primary production bottleneck encountered on large-scale 2000 L glass-lined reactors is the exotherm during hydrochloric acid salt formation; the rate of addition of concentrated HCl (36% w/w) must be limited to 1.2 L/min to maintain a reaction mass temperature below 45 °C, beyond which epimerization at C-1 of the pyrrolidine ring generates the D-erythro-D-galacto impurity at levels exceeding 0.15%.

    Container-Closure System Selection and Long-Term Stability Profile

    The hydrochloride monohydrate’s inherent acidity (pKa of conjugate acid 7.6) and hygroscopicity impose constraints on primary packaging. In double polyethylene bags inside aluminium foil laminate drums, the desiccant system — typically silica gel packets meeting MIL-D-3464E Type II — must maintain headspace relative humidity below 30% at 25 °C; otherwise, a 0.3% moisture uptake over 36 months correlates with a 2.7% loss in chromatographic purity, primarily due to hydrolysis of the thioglycosidic bond yielding methyl α-thiogalacto-octopyranoside. For ready-to-use injectable vials, Type I borosilicate glass per USP 〈660〉 with a fluoropolymer-laminated bromobutyl rubber stopper (e.g., West 4023/50 Gray) is employed; the stopper’s moisture vapour transmission rate must not exceed 0.1 g/m²/day at 40 °C/75% RH over 12 months to maintain water content within specification. Accelerated stability studies conducted per ICH Q1A(R2) at 40 °C/75% RH for 6 months demonstrate a degradation rate constant kobs of 0.0023 day⁻¹ for lincomycin B-related impurities, with the primary degradant identified as 1-demethylthio-1-hydroxy-lincomycin by LC-QTOF mass spectrometry with m/z 413.2285 [M+H]⁺.

    Differences from other thio-glycoside antibiotics extend to regulatory starting materials. The supply chain for lincomycin hydrochloride monohydrate begins with a fermentation broth of Streptomyces lincolnensis var. lincolnensis ATCC 25466, yielding crude lincomycin A of 85–92% purity after ion-exchange chromatography on a Diaion HP20 resin column with 1200 L bed volume. The subsequent selective crystallisation of the hydrochloride monohydrate from an aqueous acetone mixture (3:1 v/v acetone:water) at 5 °C over 12 h removes the co-produced lincomycin B (desmethyl analogue) to below 1.0%, a step not required for clindamycin, where the chloro substituent dramatically improves crystallisation selectivity. Manufacturers handling this intermediate must validate absence of clindamycin cross-contamination via a specific HPLC method with a limit of quantitation of 0.01%, as the presence of the chlorinated analogue at trace level alters the MIC profile of the final product and constitutes a GMP deviation under 21 CFR 211.176 (penicillin and non-penicillin beta-lactam cross-contamination guidance applied analogously to lincosamides).