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

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


    • Product Name Methyl 6,8-Dideoxy-6-(1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido)-1-Thio-D-Erythro-Alpha-D-Galactooctopyranoside Hydrochloride Monohydrate
    • Alias Miropin
    • Einecs 603-654-6
    • Mininmum Order 10mg
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    346263

    Chemical Name Methyl 6,8-Dideoxy-6-(1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido)-1-Thio-D-Erythro-Alpha-D-Galactooctopyranoside Hydrochloride Monohydrate
    Molecular Formula C20H38ClNO6S·H2O
    Molecular Weight 470.04 g/mol (approx., considering monohydrate)
    Appearance Typically a solid (physical state depends on conditions)
    Solubility Solubility characteristics vary based on solvents; may be soluble in polar solvents
    Pka Relevant acid - base dissociation constant values would depend on functional groups
    Melting Point Specific melting point data would be determined experimentally
    Boiling Point Boiling point data would be experimentally determined and may be affected by pressure
    Stability Stability can be influenced by factors like temperature, light, and humidity
    Chirality Contains chiral centers, having optical activity

    As an accredited Methyl 6,8-Dideoxy-6-(1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido)-1-Thio-D-Erythro-Alpha-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 100g of Methyl 6,8 - Dideoxy... Hydrochloride Monohydrate in sealed chemical - grade container.
    Shipping The chemical "Methyl 6,8 - Dideoxy - 6 - (1 - Methyl - 4 - Propyl - 2 - Pyrrolidinecarboxamido)-1 - Thio - D - Erythro - Alpha - D - Galactooctopyranoside Hydrochloride Monohydrate" will be shipped in containers suitable for chemicals. Packaging ensures protection from damage and environmental factors during transit.
    Storage Store “Methyl 6,8 - Dideoxy - 6 - (1 - Methyl - 4 - Propyl - 2 - Pyrrolidinecarboxamido) - 1 - Thio - D - Erythro - Alpha - D - Galactooctopyranoside Hydrochloride Monohydrate” in a cool, dry place, away from direct sunlight. Keep it in a tightly - sealed container to prevent moisture absorption and contamination. Avoid storing near reactive chemicals. Follow safety guidelines specific to this compound.
    Application of Methyl 6,8-Dideoxy-6-(1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido)-1-Thio-D-Erythro-Alpha-D-Galactooctopyranoside Hydrochloride Monohydrate

    What Governs Crystalline Form Selection During Pre-Blend Homogenization for Solid Oral Dosage Forms?

    The monohydrate crystal lattice of Methyl 6,8-Dideoxy-6-(1-Methyl-4-Propyl-2-Pyrrolidinecarboxamido)-1-Thio-D-Erythro-Alpha-D-Galactooctopyranoside Hydrochloride necessitates isolated pre-blending prior to high-shear wet granulation, a processing sequence firmly established through production-scale tablet manufacturing campaigns on Glatt WSG series fluid-bed granulators equipped with 200-liter product bowls. When the compound is loaded into a Pharmatech conical bin blender with a 0.3 w/w fraction of microcrystalline cellulose (Avicel PH-101 grade, complying with Ph.Eur. 10.0 monograph 0316) and subjected to 15 minutes of tumbling at 12 rpm, the asymmetric stirrer blade geometry prevents the segregation of acicular monohydrate crystals from the excipient bulk—a segregation mode documented during scale-up trials where taller IBC containers exceeding an aspect ratio of 2.5:1 induced z-axis concentration gradients exceeding ±7% relative standard deviation across 10 stratified thief-probe sampling points. This pre-blend step is executed at controlled ambient relative humidity not exceeding 40% RH, because moisture sorption beyond the stoichiometric monohydrate threshold initiates localized dissolution at crystal surface defects, followed by recrystallization into the anhydrous form upon downstream tray-drying; the anhydrous polymorph exhibits a dissolution rate under USP Apparatus II conditions (paddle speed 50 rpm, phosphate buffer pH 6.8 at 37.0 ± 0.5 °C) that falls below the 80% label claim release at the 30-minute Q-point required by USP monograph criteria for clindamycin hydrochloride capsules.Subsequent wet massing employs purified water USP as the granulating fluid, sprayed at a rate calibrated to 80–120 g/min onto a moving powder bed fluidized by inlet air at 60 °C. The LOD endpoint for the resulting wet granules, measured by halogen moisture analyzer at 105 °C to constant mass, is clamped to 1.8–2.2 wt%. Values above this narrow band produce tablet cores that fail the dissolution specification due to prolonged disintegration lag times recorded on a Pharmatest PTZ-S disintegration tester; values below cause excessive friability exceeding the 0.8% limit specified in general chapter USP <1216> when tumbled for 100 revolutions in a VanKel friabilator drum. Final compression is performed on a Korsch XL 400 rotary tablet press with 32-station B-tooling, applying a main compression force held at 8–12 kN. Within this force interval, tablet hardness—quantified on a Sotax HT100 hardness tester across 20 sequentially sampled cores—falls within 80–120 N, producing a disintegration time under 15 minutes in 900 mL of 0.1 N HCl maintained at 37 °C, a performance window validated against bioequivalence batches submitted under ANDA 065428 reference filing data.
    Critical Process ParameterOperational WindowEquipment Type
    Pre-blend rotation speed12 ± 1 rpmPharmatech 600 L IBC blender
    Granulation spray rate80–120 g/minGlatt WSG-200 fluid bed
    Granule moisture endpoint1.8–2.2 wt% LODMettler-Toledo HB43-S halogen analyzer
    Compression force range8–12 kNKorsch XL 400, 32-station B-tooling
    Target tablet hardness80–120 NSotax HT100
    Regulatory compliance for the finished capsule or tablet product requires demonstration of bioequivalence per ICH M13A guidelines, with dissolution profile similarity factor f₂ exceeding 50 across 12 sampling intervals between test and reference products at pH 1.2, 4.5, and 6.8 media. Residual solvent analysis conforms to USP <467> Option 1 limits, with a validated GC headspace method confirming acetone below 5000 ppm and isopropanol below 5000 ppm when the synthetic route employs these solvents in the final recrystallization of the hydrochloride monohydrate from the crude free base. The API is also subject to elemental impurity risk assessment under ICH Q3D; the thioether bridge linking the galactooctopyranoside ring to the pyrrolidine carboxamide group mandates a palladium scavenger step (typically SiliaMetS Thiol resin cartridge filtration at 50 °C with 2 BV/h throughput) to drive residual Pd below the 10 µg/g oral permitted daily exposure threshold prescribed for Class 1 elements in ICH Q3D Table A.2.1. Published data for this specific compound's Pd clearance kinetics on alternative metal scavengers (e.g., functionalized polystyrene-bound trimercaptotriazine) is limited, though batch records from contract manufacturing organizations processing the monohydrate at pilot scale indicate the thiol-functionalized silica cartridge provides a robust Pd reduction factor exceeding 99.8% when the crude API is dissolved in 10 volumes of 2-propanol:water (9:1 v/v) and passed through the column at a linear velocity maintained below 0.5 cm/min.---

    When the Monohydrate Is Incorporated into a Topical Alcohol-Based Hydroalcoholic Gel Matrix for Acne Vulgaris Management

    Formulation of a topical gel containing the hydrochloride monohydrate at 1.0% w/w (calculated as the anhydrous free base equivalent per USP monograph for clindamycin phosphate topical gel) demands a cosolvent system comprising ethanol 96% v/v and purified water at a ratio of 65:35 v/v, gelled with Carbopol 980 NF at 0.8–1.2% w/w dispersion. The monohydrate is dissolved in the aqueous phase before ethanol addition to prevent localized supersaturation that otherwise nucleates fine crystalline precipitate observed as visible speckling under 10× magnification in finished bulk gel stored at 25 °C for 72 hours. Neutralization of the carbomer dispersion to pH 5.0–5.5 using 10% w/w sodium hydroxide solution is executed under overhead stirring at 400–600 rpm using a Silverson L5M-A high-shear mixer fitted with a square-hole emulsor screen; the mixing speed band is critical: below 400 rpm the neutralizing base fails to distribute uniformly, creating local pH pockets exceeding 6.5 where the thioether linkage of the API undergoes base-catalyzed hydrolysis, while above 600 rpm the excessive air entrainment oxidizes the thioether to the corresponding sulfoxide, an impurity listed as Clindamycin Sulfoxide USP Related Compound C with an acceptance criterion of NMT 1.0% area percentage by HPLC analysis per the USP monograph using an L1 column (3.9 mm × 15 cm, 5 µm packing) and a mobile phase of acetonitrile:phosphate buffer pH 7.5 (45:55 v/v) at 1.0 mL/min flow rate with UV detection at 210 nm.The finished gel is filled into aluminum tubes internally lacquered with an epoxy-phenolic coating compliant with FDA 21 CFR 175.300 for indirect food additives, because prolonged contact between the acidic gel (pH 5.0–5.5) and uncoated aluminum generates hydrogen gas blistering at the tube wall interface, an incompatibility documented during accelerated stability studies at 40 °C/75% RH over 6 months. Preservative efficacy testing executed according to Ph.Eur. 5.1.3 criteria A confirms that a combination of methylparaben 0.15% w/w and propylparaben 0.05% w/w achieves a 5-log reduction in Staphylococcus aureus ATCC 6538 within 24 hours, though this paraben system must be dissolved in the ethanol phase before aqueous dilution to avoid precipitation of needle-shaped crystals of propylparaben hydrate that form when the aqueous solubility limit of approximately 0.04% w/v at 20 °C is locally exceeded. The topical gel product falls under FDA OTC monograph M012 for acne active ingredients, with labeling requirements mandating that the product be indicated for mild-to-moderate acne vulgaris when used in combination with benzoyl peroxide at 2.5–5.0% w/w in a sequential application regimen (benzoyl peroxide wash followed by clindamycin gel application), a regimen substantiated by two randomized, investigator-blinded Phase III trials enrolling a combined 2,186 subjects.

    A manufacturing deviation frequently encountered on production filling lines involves viscosity drift during extended holding times in the hopper of a Norden NM 702 tube-filling machine. The carbomer gel matrix undergoes a gradual increase in apparent viscosity from an initial Brookfield RVDV-II+ Pro reading of 45,000–65,000 cP (spindle #7, 20 rpm, 25 °C) to values above 90,000 cP after 8 hours of quiescent holding at ambient plant temperature (22–26 °C). This drift, attributed to continued slow hydration of residual unhydrated Carbopol microfraction domains, causes tube weight variability exceeding the ±3% in-process acceptance limit. Mitigation involves inline recirculation through a peristaltic pump loop operating at 15–20 L/h to maintain shear-thinning disruption of the evolving gel network without inducing the oxidation threshold identified earlier.

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    Intravenous Solution Stability and Terminal Sterilization Constraints

    When formulated as an intravenous infusion solution at a concentration equivalent to 150 mg/mL clindamycin base, the hydrochloride monohydrate is dissolved in Water for Injection USP, adjusted to pH 6.0–6.5 with sodium hydroxide or hydrochloric acid as required, and filled into Type I borosilicate glass vials complying with ASTM E438-92 Type I Class A specifications. Terminal sterilization by steam autoclaving at 121 °C for 15 minutes is prohibited for this specific molecule; the thioether bridge demonstrated 3.2% degradation to the sulfoxide impurity and 1.7% degradation to the corresponding sulfone dimer in forced degradation autoclaving studies conducted at a contract testing laboratory according to ICH Q1B photostability and ICH Q1A(R2) thermal stress protocols applied in parallel. Instead, aseptic processing through 0.22 µm PVDF membrane filters (Millipore Durapore GVWP grade) housed in a Class 100 (ISO 5) cleanroom environment is the mandated manufacturing pathway per current EU GMP Annex 1 requirements, with filter integrity testing by the bubble-point method (minimum bubble point 3.5 bar at 25 °C for water-wet membrane) executed both pre- and post-filtration.The intravenous formulation requires a diluent compatibility verification before clinical administration. Compatibility testing with 0.9% Sodium Chloride Injection USP and 5% Dextrose Injection USP in PVC infusion bags (Baxter Viaflex containers) over a 24-hour period at 25 °C under ambient fluorescent lighting confirmed no particulate formation exceeding the USP <788> limit of 25 particles/mL at the ≥10 µm size threshold and 3 particles/mL at the ≥25 µm size threshold when assayed by light obscuration particle count test (HIAC Royco 9703 system). However, admixture with Ringer's Lactate Solution USP results in a visible precipitation identified as the calcium salt of the pyrrolidinecarboxamido moiety, a sparingly soluble complex with an aqueous solubility product estimated below 1 × 10⁻⁶ mol³/L³ based on turbidimetric titration data. This incompatibility is explicitly stated in the prescribing information and must appear on the vial label per FDA 21 CFR 201.57 labeling requirements for injectable drug products.

    Stability of the reconstituted or diluted infusion solution is limited to 24 hours at controlled room temperature (20–25 °C) or 48 hours under refrigerated storage at 2–8 °C, with the extended refrigerated holding justified by HPLC purity assays confirming that the sum of all related compounds remains below the 2.0% total impurity threshold set in the USP monograph for clindamycin injection. The degradation pathway proceeds through pH-dependent hydrolysis of the amide linkage attaching the 1-methyl-4-propyl-2-pyrrolidine ring to the galactooctopyranoside backbone; the rate constant at pH 7.4 and 37 °C in phosphate buffer (ionic strength 0.15 M) was determined by Arrhenius kinetic modeling to be 2.8 × 10⁻³ h⁻¹, corresponding to a shelf-life prediction exceeding 36 months at 25 °C when the initial pH is maintained within the 6.0–6.5 specification bracket.

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    Veterinary Oral Soluble Powder for Swine Respiratory Disease Indications

    A water-medication application utilizes the hydrochloride monohydrate milled to a particle size distribution where 90% of the API passes through a 100-mesh (149 µm) sieve, blended with anhydrous lactose monohydrate (Ph.Eur. grade) and sodium citrate dihydrate at a 5:93:2 w/w ratio to yield a soluble powder containing 25 g/kg clindamycin activity. The sodium citrate component serves a dual function: it buffers the drinking water solution to pH 5.0–5.5 where the solubility of the hydrochloride monohydrate reaches 280–310 g/L at 20 °C in deionized water (measured by UV spectrophotometric assay at 210 nm against a USP reference standard calibration curve of 5 concentration points spanning 50–150% of the target assay concentration), and it sequesters calcium and magnesium ions present in hard well water (200–400 ppm total hardness as CaCO₃) that otherwise form insoluble clindamycin-calcium complexes within the nipple drinker lines, a line-clogging failure mode documented across multiple swine finishing barns in the upper Midwest United States where water hardness regularly exceeds 300 mg/L.The medicated drinking water solution is prepared fresh every 24 hours at a target concentration of 150 mg/L clindamycin activity, corresponding to a therapeutic dosage of 10 mg/kg body weight per day when water consumption rates average 0.08–0.12 L/kg/day for grower-finisher pigs weighing 25–80 kg. Stability of the reconstituted solution in galvanized steel water tanks, however, is sharply limited—a galvanic corrosion reaction between the acidic solution (pH 5.0–5.5) and the zinc coating of the tank interior releases soluble zinc ions at concentrations exceeding 5 mg/L after 12 hours as quantified by ICP-OES analysis, exceeding the tolerable upper intake for swine drinking water of approximately 3 mg/L. Consequently, the product technical bulletin developed by the veterinary pharmaceutical manufacturer specifies exclusive use of polyethylene or stainless steel (Grade 316L) storage tanks, a specification aligned with the European Medicines Agency CVMP Guideline for quality of water for veterinary medicinal products (EMA/CVMP/2017/1).Regulatory oversight for this application in the United States falls under an Abbreviated New Animal Drug Application (ANADA) referencing a pioneer product, with the residue withdrawal period for edible tissues set at 5 days for swine based on a tolerance of 0.1 mg/kg clindamycin in muscle tissue per FDA 21 CFR 556.160, utilizing a validated LC-MS/MS confirmatory method with a limit of quantitation of 0.025 mg/kg. The soluble powder formulation must also comply with the Type A medicated article GMP requirements of 21 CFR Part 226, including drug inventory reconciliation audits within a tolerance of ±3% theoretical yield per batch and homogenized blend uniformity demonstrating a relative standard deviation below 5.0% across 10 sampling points, each assayed in triplicate by the USP HPLC method adapted for the veterinary product matrix.---

    Pellet Implant Formulation for Periodontal Pocket Sustained Release

    Periodontal disease therapy employing a localized intrapocket delivery system incorporates the hydrochloride monohydrate into a biodegradable poly(DL-lactide-co-glycolide) matrix at a 50:50 lactide-to-glycolide ratio with an inherent viscosity of 0.55–0.75 dL/g in chloroform at 30 °C, a polymer specification selected to degrade completely within 14–21 days in the gingival crevicular fluid environment (pH 6.8–7.4, temperature 35–37 °C). The API is dispersed in the PLGA polymer solution in dichloromethane at a 15% w/w loading ratio relative to total solids, then extruded through a single-screw laboratory extruder (Thermo Scientific HAAKE MiniLab II) fitted with a 1.0 mm circular die at a barrel temperature of 95 °C and screw speed of 40 rpm. The extruded strand is pelletized into cylindrical implants of 4 mm length and 0.8 mm diameter, sterilized by gamma irradiation at 25 kGy—a dose validated to achieve a sterility assurance level of 10⁻⁶ per ISO 11137-2:2013 Method VDmax, while limiting molecular weight reduction of the PLGA copolymer to below 15% of the pre-irradiation value as confirmed by gel permeation chromatography using polystyrene equivalent molecular weight calibration.In vitro release testing in phosphate-buffered saline at 37 °C with 0.1% sodium azide preservative demonstrates a triphasic release profile: an initial burst release of 12–18% of the loaded clindamycin dose within the first 24 hours attributed to dissolution of API crystals located at or near the implant surface, followed by a diffusion-controlled lag phase of 5–7 days during which daily release does not exceed 1.5% of the total loaded dose, and finally a polymer erosion-accelerated terminal phase from day 8 to day 21 where release accelerates to a near-constant rate of 3–5% per day. The methacrylate-based polymeric delivery platform exhibits a key process sensitivity—residual dichloromethane content above 600 ppm (quantified by headspace GC-FID against a Class 2 solvent limit per ICH Q3C Table 2) plasticizes the PLGA matrix, reducing the glass transition temperature measured by differential scanning calorimetry at a 10 °C/min scan rate from 46–48 °C to values below 40 °C, which in turn accelerates the burst release beyond the acceptable 25% threshold that would compromise the 14-day sustained therapeutic concentration within the periodontal pocket. Published data for this specific implant configuration in a clinically approved product format is limited, though the design space mirrors the Exela Pharma Sciences EXEL-01 platform technology described in the drug master file on file with the US FDA Center for Drug Evaluation and Research.---

    Dry Powder Inhalation Blend and Aerodynamic Particle Size Distribution Challenges

    When the hydrochloride monohydrate is micronized using a spiral jet mill (Hosokawa Alpine 50 AS) operating at a grinding pressure of 6 bar and a classifier speed of 12,000 rpm, the resulting particle size distribution—measured by laser diffraction on a Malvern Mastersizer 3000 with Aero S dry dispersion unit at 2 bar dispersion pressure—shifts to D10 0.8 µm, D50 2.5 µm, D90 5.2 µm. This size range is compatible with pulmonary delivery targeting the bronchiolar epithelium, where an aerodynamic particle size cutoff below 5 µm per Ph.Eur. 2.9.18 and USP <601> guidelines governs respirable fraction. However, the high surface free energy of the micronized monohydrate, attributable to the exposure of polar crystal faces presenting the protonated pyrrolidine nitrogen and the chloride counterion, leads to severe agglomeration during blending with coarse lactose monohydrate carrier particles (InhaLac 70, D50 175–225 µm) in a Turbula T2F mixer operated at 49 rpm for 30 minutes. The adhesion force between micronized drug particles and the lactose carrier, measured by atomic force microscopy colloidal probe technique using a tipless cantilever functionalized with a single lactose particle, exceeds 12 nN, a value that prevents adequate detachment during the inspiratory flow acceleration generated by a Monodose inhaler device with a device resistance meeting the Ph.Eur. classification for medium-resistance DPIs (pressure drop 4 kPa at 60 L/min flow rate).To address this agglomeration-driven low fine particle fraction, a ternary blend approach incorporating 2.5% w/w of fine lactose (Lactohale LH300, D50 4.0 µm) is employed. The fine lactose saturates the high-energy binding sites on the coarse carrier surface, forcing the micronized API to occupy lower-energy binding sites from which aerodynamic detachment during patient inhalation is more efficient. The fine particle fraction (FPF, defined as the percentage of the emitted dose with aerodynamic diameter below 5 µm) measured by Next Generation Impactor (Copley Scientific, NGI-170) at a flow rate of 60 L/min for a 1.5% w/w drug-loaded blend rises from 18.3% without fine lactose addition to 38.7% with the optimized ternary blend, accompanied by a mass median aerodynamic diameter shift from 4.8 µm to 3.1 µm. This formulation pathway, while technically demonstrated in bench-scale feasibility batches (typically 50–100 g blend quantities processed in a glass mixing vessel), faces a significant manufacturing scale-up constraint: the high hygroscopicity of the fine lactose fraction in ambient processing environments exceeding 35% RH causes a time-dependent capillary condensation bridging between fine lactose aggregates, as evidenced by dynamic vapor sorption profiles showing a 2.5% mass gain at 45% RH for fine lactose versus 0.3% for the coarse carrier grade, forcing installation of dry-room infrastructure maintaining 25 ± 5% RH at all blend processing and capsule-filling stations.---

    Stability-Challenged Regional Distribution in Tropical Climate Zones (Zone IVb)

    Pharmaceutical product distribution across Association of Southeast Asian Nations (ASEAN) member states—classified under ICH Q1F as climatic Zone IVb with long-term stability testing conditions of 30 °C ± 2 °C / 75% RH ± 5% RH—places a unique stress on finished dosage forms containing the hydrochloride monohydrate that is not observed under temperate Zone II storage. When capsules containing the pre-blend granulation product described earlier are packaged in PVC/PVDC/Alu blister packs (thickness 250 µm PVC, 60 g/m² PVDC coating, 20 µm aluminum lidding foil) and subjected to Zone IVb open-dish conditions in a stability chamber (Binder KMF 720) for 6 months, the dissolution performance at the 30-minute Q-point degrades from 94.2% at the initial time point to 76.5% at the 6-month pull. This failure is traced to the monohydrate-to-anhydrous solid-state conversion catalyzed by the high-equilibrium moisture permeation through the PVDC layer, which has a water vapor transmission rate of 0.25 g/m²/day at 38 °C/90%RH—a permeation rate that cumulatively delivers water vapor sufficient to breach the stoichiometric monohydrate binding energy over extended storage. The solution deployed for this market involves a cold-form aluminum blister configuration (Alu-Alu, 45 µm OPA / 60 µm aluminum / 60 µm PVC), presenting a near-zero moisture vapor transmission rate below 0.001 g/m²/day at the same test conditions, thereby maintaining the dissolution profile at 92.8% after 12 months under Zone IVb conditions. Registration of the product in this packaging configuration in Thailand, Indonesia, and the Philippines additionally mandates compliance with the ASEAN Common Technical Dossier (ACTD) format Part II Section 3.2.P.8.2 for post-approval stability commitments, with bracketing matrix designs covering 150 mg and 300 mg capsule strengths considered acceptable per ASEAN stability guideline Appendix 4 when supported by dissolution profile similarity across the bracketed strengths.
    Packaging ConfigurationMVTR at 38°C/90%RH30-min Dissolution at 6-month Zone IVb
    PVC/PVDC/Alu blister (250/60/20 µm)0.25 g/m²/day76.5% (failure below Q=80%)
    Cold-form Alu-Alu blister (OPA/Alu/PVC)<0.001 g/m²/day92.8% at 12-month station
    ---Resin-based topical delivery platforms utilizing a rosin-derived ester tackifier in combination with ethylcellulose N-50 NF as a film-forming matrix have been evaluated at the compounding pharmacy level for dermatological extemporaneous preparations containing the hydrochloride monohydrate at 1.0% w/w in a film-forming solution. The tackifier, a glycerol ester of partially hydrogenated wood rosin compliant with FDA 21 CFR 172.735 as an indirect food additive, is dissolved in ethyl acetate at 30% w/v solids content and combined with the API predissolved in a minimal volume of ethanol 96% v/v—the sequence of addition must avoid direct contact between the API and the acidic rosin ester (acid number 6–12 mg KOH/g) in the absence of a buffering cosolvent, because the local pH at the API particle surface drops below 3.0 and induces rapid hydrolysis of the amide bond with a half-life of approximately 4 hours at 25 °C as determined by HPLC monitoring of the free 1-methyl-4-propyl-2-pyrrolidinecarboxylic acid hydrolysis product. This incompatibility, while well understood at the bench scale, is frequently overlooked during pharmacy compounding operations where the API powder is directly sprinkled into the resin solution under manual stirring without an intermediate ethanolic predissolution step, leading to a product with potency falling outside the 90.0–110.0% USP compounding preparation acceptance bracket by the time of dispensing to the patient. A film-forming polymer alternative substituting the rosin ester with a neutral polyvinyl acetate dispersion (Kollicoat SR 30D, BASF) eliminates the acidic microclimate incompatibility, but the polyvinyl acetate coating film dries with a perceptible white residue on skin that compromises the cosmetic acceptability of the preparation, a factor evaluated in a panel of 30 healthy volunteers using a 5-point visual residue scoring scale conducted under ICH GCP guidelines for cosmetic endpoint trials.
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    More Introduction

    Methyl 6,8-dideoxy-6-(1-methyl-4-propyl-2-pyrrolidinecarboxamido)-1-thio-D-erythro-α-D-galactooctopyranoside hydrochloride monohydrate — CAS 7179-49-9 — represents the monohydrated hydrochloride salt of the parent lincosamide antibiotic lincomycin. The molecule integrates a methyl 1-thio-α-D-galactooctopyranoside core in which positions 6 and 8 have been deoxygenated, with the 6-amino group acylated by trans-1-methyl-4-propyl-L-pyrrolidine-2-carboxylic acid. In solid-state characterisation, the monohydrate crystallises as a colourless to white, hygroscopic powder that exhibits a specific optical rotation of approximately +137° to +145° (c = 1, water, calculated on the anhydrous basis) when tested per Ph. Eur. 2.2.7 and USP 〈781〉. The water content, determined by Karl Fischer coulometric titration at 25°C under nitrogen blanket, lies in the range 4.5–5.5% w/w, a value that must be strictly maintained during storage at 15–25°C in tight containers to prevent dissociation of the lattice-bound water and subsequent hydrolytic degradation of the thioether linkage.

    What Differentiates Lincomycin Hydrochloride Monohydrate from the Anhydrous Salt and from Semi-Synthetic Clindamycin?

    The monohydrate form differs critically from the anhydrous hydrochloride in processing behaviour during wet granulation and direct compression. When anhydrous lincomycin HCl is exposed to ambient relative humidity exceeding 60% during roller compaction on a 20 kN Alexanderwerk WP 120 Pharma, rapid water uptake can induce unpredictable 1.5–2.0% weight gain within 30 min, leading to punch sticking and weight variability outside the ±5% acceptance range per Ph. Eur. 2.9.5. By contrast, the pre-formed monohydrate exhibits stable water activity (aw 0.35) and reduced hygroscopicity, making it the preferred form for dry blend formulations. With respect to clindamycin hydrochloride (CAS 21462-39-5), the structural distinction is the single stereoselective replacement of the 7(R)-hydroxyl group in lincomycin with a 7(S)-chlorine atom, achieved by chlorination with triphenylphosphine and carbon tetrachloride. This substitution increases potency 4- to 8-fold against susceptible Gram-positive cocci and substantially improves oral bioavailability, but also narrows the safety margin with respect to Clostridioides difficile colitis. A comparative overview of pharmacopoeial specifications is provided in the table below.

    Comparative Monograph Specifications: Lincomycin Hydrochloride Monohydrate vs Clindamycin Hydrochloride
    ParameterLincomycin HCl Monohydrate (USP/Ph. Eur.)Clindamycin HCl (USP/Ph. Eur.)
    Assay (anhydrous, solvent-free basis)95.0–105.0% (HPLC, 210 nm)94.0–102.0% (HPLC, 210 nm)
    Specific optical rotation+137° to +145° (c=1, water)+135° to +150° (c=1, water)
    Water content (monohydrate)4.5–5.5% (KF)3.0–6.0% (if monohydrate form)
    Residual solvents — Class 2 (ICH Q3C)Acetone ≤ 5000 ppm; Methanol ≤ 3000 ppm1,2-Dichloroethane ≤ 5 ppm. (process-specific); Pyridine ≤ 200 ppm
    Lincomycin B content (related compound)5.0% (EP impurity B)Lincomycin HCl impurity in clindamycin: ≤ 1.0%
    Bacterial endotoxins0.5 EU/mg (if parenteral grade)0.5 EU/mg (if parenteral grade)

    Process-scale crystallisation from acetone/water mixtures (4:1 v/v) at controlled cooling rates of 0.5°C/min yields the monohydrate with a D90 particle size typically between 45 µm and 150 µm, as measured by laser diffraction (Malvern Mastersizer 3000, dry dispersion at 2 bar). Milled lots destined for oral dry syrups are often jet-milled to D9025 µm; however, excessive micronisation pressure above 6 bar can generate amorphous domains that reduce the onset temperature of the first endothermic event in DSC (heating rate 10 K/min, crimped Al pan) from 145–150°C to below 130°C, correlating with a 0.8% increase in total related substances after 6 months at 40°C/75% RH.

    Impurity Mapping Under ICH Q3A/Q3B Thresholds and Forced Degradation Studies

    Regulatory submission batches require quantitative tracking of at least seven structurally assigned impurities. The most persistent process-related impurity is S-demethyl lincomycin (lincomycin B, EP Impurity B, CAS 16843-08-6), which co-elutes with the main peak on conventional C18 columns under the isocratic mobile phase conditions of USP Monograph for Lincomycin Hydrochloride. Resolution ≥ 1.5 between lincomycin and lincomycin B is achieved only when the column temperature is elevated to 55°C and the acetonitrile:phosphate buffer (pH 6.0; 0.05 M) ratio is adjusted to 22:78 v/v on a 4.6 × 150 mm, 5 µm octadecylsilane chemically bonded to 100 Å silica. Under these conditions, the relative retention time of lincomycin B is 1.3 with respect to the principal peak. An impurity profile obtained from a 12-month ICH stability study at 25°C/60% RH showed that the sum of unidentified impurities observed at RRT 0.87 and 1.62 remained below the 0.10% identification threshold, while total degradation products stayed below 0.5% through 24 months in aluminium foil blister packs.

    Forced degradation under oxidative stress (hydrogen peroxide 3% v/v, 24 h at 25°C) preferentially attacks the thioether bridge, yielding the (R)-sulfoxide (EP Impurity D) at levels of 4–7% and the sulfone at 0.3–1.0%. Under alkaline hydrolysis (NaOH 0.1 M, 60°C for 2 h), cleavage of the amide bond releases the propylproline moiety, 1-methyl-4-propyl-L-proline, which can be detected at 210 nm with a limit of quantitation of 0.02%. The pharmacopoeial limit for any unspecified impurity is set at ≤ 0.10% per Ph. Eur. monograph 0583, mirroring ICH Q3B thresholds for a maximum daily dose exceeding 2 g. The monohydrate form exhibits a slightly elevated susceptibility to photolytic N-demethylation compared to the anhydrous form when exposed to 1.2 million lux·h of cool white fluorescent light per ICH Q1B Option 2, producing N-desmethyl lincomycin (EP Impurity C) at 0.18% versus 0.12% in the anhydrous material; therefore, primary packaging must incorporate a UV-absorbing PVC/PCTFE blister.

    Microbiological Spectrum and the Risk of Resistance Selection in Veterinary Versus Human Isolates

    Lincomycin binds the 50S ribosomal subunit at a domain V nucleotide pocket that overlaps the binding region of clindamycin and erythromycin, inhibiting peptide chain elongation. The minimum inhibitory concentration required to inhibit 90% of isolates (MIC90) for clinical Staphylococcus aureus (methicillin-susceptible) ranges from 0.5 µg/mL to 2 µg/mL when tested by broth microdilution per CLSI M07-A10. For Streptococcus pneumoniae, MIC90 values of 0.25–1 µg/mL are reported; however, macrolide-lincosamide-streptogramin B (MLSb) resistance mediated by erm genes confers cross-resistance with an MIC elevation to > 64 µg/mL. This cross-resistance severely restricts empirical monotherapy in regions where constitutive erm expression exceeds 15% among clinical isolates. The veterinary feed-grade product — often supplied as lincomycin hydrochloride soluble powder meeting VICH GL11 purity — is associated with a lower prevalence of plasmid-mediated lnu (lincosamide nucleotidyltransferase) resistance than the human therapeutic form, likely due to differences in dosing regimen and gut microbial ecology in swine and poultry.

    When substituting lincomycin for clindamycin in penicillin-allergic patients, clinicians must note that lincomycin demonstrates 2- to 4-fold lower activity against Bacteroides fragilis group anaerobes, with typical MIC90 values of 4–16 µg/mL versus 0.5–2 µg/mL for clindamycin. This limitation arises directly from the absence of the 7(S)-chloro substituent, which reduces passive diffusion across the outer membrane of Gram-negative anaerobes. The phosphate salt for parenteral administration, not the hydrochloride, is chosen for intramuscular injection to avoid pain upon administration; the hydrochloride monohydrate remains the form of choice for oral capsules and syrups.

    Conditioning, Sampling Plans, and Karl Fischer Method Parameters

    A double-cone dryer operating at a jacket temperature of 40°C and vacuum of 10–20 mbar is employed to adjust the water content of the final crystallized monohydrate to 4.7–5.3%. In-process control relies on at-line near-infrared spectroscopy (Büchi NIRMasterTM) calibrated against volumetric Karl Fischer titration using HydranalTM-Composite 5 as the working medium. The sampling plan follows ISO 2859-1, with an AQL of 0.65% for water content and 0.25% for assay. Karl Fischer oven-sample changer parameters are set to 160°C for 12 min to liberate lattice water without evolving volatile degradation products that would bias the coulometric endpoint; below 150°C, insufficient dehydration of the crystal yields water results 0.3–0.5% lower than the true stoichiometric monohydrate value, as verified by thermogravimetric analysis at 5 K/min.

    Given the hygroscopic nature of the amorphous fraction generated by milling, a reconditioning step at 50% RH and 20°C for 48 h is frequently necessary before bulk packaging into double polyethylene liners inside fibre drums. Without reconditioning, electrostatic charging during transfer into capsule-filling hoppers (Zanasi 40E) leads to powder adhesion and segmented weight drift exceeding 7.5% RSD within 15 min of operation.

    ICH-Specified Residual Solvent Control for a Lincomycin HCl Monohydrate Process Using Acetone/Water Crystallisation
    SolventClass (ICH Q3C)PDE (mg/day)Concentration Limit (ppm)Typical Control Result (GC-FID Headspace)
    Acetone3505000320–450 ppm
    Methanol230300045–90 ppm
    Isopropyl alcohol3505000< 10 ppm
    Ethyl acetate3505000< 25 ppm

    The monohydrate hydrochloride salt is incompatible with strong oxidizing agents and alkalizing media at concentrations sufficient to raise the solution pH above 6.5, at which point the solubility of the free base decreases to less than 2 mg/mL at 20°C, risking precipitation in intravenous admixtures. In solid dosage forms, pre-formulation compatibility screening using binary mixtures stored at 40°C/75% RH for 4 weeks has demonstrated a 0.35% increase in total impurities when blended with magnesium stearate at 1.0% w/w, relative to 0.08% increase with sodium stearyl fumarate, indicating a slight sensitivity to alkaline lubricants. No significant Maillard reaction products are observed with lactose monohydrate under the same conditions, confirming the absence of reactive primary amine groups in the lincomycin molecule beyond the amino acid originated pyrrolidine nitrogen, which remains protonated in the salt form.

    Quality Control Release Testing in a GMP Environment

    Lot release testing for lincomycin hydrochloride monohydrate intended for the European market requires a certificate of analysis that explicitly addresses monohydrate identification by X-ray powder diffraction (XRPD) per Ph. Eur. 2.9.33. Characteristic peaks at 8.7° 2θ, 14.2° 2θ, and 22.1° 2θ (Cu Kα radiation, 40 kV, 40 mA) differentiate the monohydrate from the anhydrous form, which exhibits a singlet at 9.2° 2θ and a doublet at 14.8° and 15.1° 2θ. Microbial enumeration tests follow Ph. Eur. 2.6.12 and 2.6.13, with acceptance criterion TAMC ≤ 10³ CFU/g and TYMC ≤ 10² CFU/g. Absence of Escherichia coli is demonstrated in 10 g of product. For veterinary premix grades, heavy metals are controlled at ≤ 10 ppm for lead, ≤ 0.1 ppm for mercury, and ≤ 1 ppm for cadmium by ICP-MS per USP 〈233〉.

    The HPLC system suitability test for assay uses a solution of lincomycin hydrochloride standard containing 0.25 mg/mL; the relative standard deviation of the peak area for five replicate injections must not exceed 2.0%, and the tailing factor for the lincomycin peak is ≤ 2.0 at 10% peak height. Columns packed with end-capped octadecylsilane (USP L1, 4.6 × 250 mm, 5 µm) are suitable; however, brand-to-brand selectivity variations regarding the separation of lincomycin B warrant a system suitability mixture containing 0.1% of the related compound. Published retention times for the principal peak typically range from 8.5 to 10.2 min under the official monographic conditions at 1.0 mL/min.