| HS Code | 928995 |
| Product Name | Menantine Hydrochloride (Memantine Hydrochloride) Pharma Grade API |
| Chemical Name | 1-Amino-3,5-dimethyladamantane hydrochloride |
| Cas Number | 41100-52-1 |
| Molecular Formula | C12H21N·HCl |
| Molecular Weight | 215.76 g/mol |
| Appearance | White or almost white crystalline powder |
| Assay | ≥99.0% |
| Grade | Pharma Grade / API |
| Pharmacopoeia | USP/EP/BP/IP |
| Solubility | Freely soluble in water; soluble in ethanol; practically insoluble in acetone |
| Melting Point | Approximately 292°C with decomposition |
| Therapeutic Class | NMDA receptor antagonist |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Route Of Administration | Oral and Injectable |
| Storage | Cool, dry, protected from light, tightly closed containers |
| Packaging | 25 kg fiber drum with double polyethylene bags |
| Shelf Life | 2 to 3 years when stored properly |
| Regulatory Status | Active Pharmaceutical Ingredient (API) |
As an accredited Menantine Hydrochloride Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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For 5 mg and 10 mg immediate-release tablet cores, direct compression of memantine hydrochloride is governed less by API chemical instability than by particle-size distribution, electrostatic adhesion, and blend segregation under low-dose conditions. Incoming API lots are released against the current USP-NF Memantine Hydrochloride monograph, with residual solvent control under ICH Q3C Table 2, elemental impurity screening under ICH Q3D Table 5.2, and GMP accountability under 21 CFR 211.84 and 21 CFR 211.110. The formulation addition ratio is set by the 5 mg/250 mg core and 10 mg/250 mg core configurations, corresponding to 2.0% w/w and 4.0% w/w active fractions, while a working range of 1.5–5.0% w/w is maintained because lower fractions amplify content uniformity risk and higher fractions can reduce tablet hardness when microcrystalline cellulose is the dominant filler. For processing, the API is first passed through a 0.8 mm screen on a cone mill, pre-blended with an equal mass of microcrystalline cellulose in a 100 L bin blender at 10–12 rpm for 10 min, then mixed with croscarmellose sodium and pregelatinized starch for 20 min; lubrication with 0.5% w/w magnesium stearate is limited to 3–5 min to avoid delayed dissolution. Compression on a 16-station B-tooling rotary tablet press at 7–12 kN main compression force produces 60–90 N tablet hardness and friability below 0.8% w/w per USP <1216>; disintegration is determined per USP <701> in distilled water at 37±2°C, with acceptance not more than 15 min. Dissolution is run per USP <711> Apparatus II at 50 rpm in 900 mL of 0.1 N HCl, with a typical acceptance of Q=80% at 30 min for immediate-release cores. Terminal finished product types are round biconvex film-coated tablets of 5 mg and 10 mg, packaged in HDPE bottles with desiccant and child-resistant closures. Operational boundary: when ambient relative humidity exceeds 60%, the API is tray-dried at 40–50°C for 4–6 h before sieving, and lubrication above 1.0% w/w magnesium stearate is avoided because it produces measurable disintegration delay and dissolution failures at the 30 min sampling point.
Extended-release memantine hydrochloride capsules are produced as polymer-coated pellets filled into hard gelatin or hypromellose capsules; unit strengths of 7 mg, 14 mg, 21 mg, and 28 mg memantine HCl are obtained by varying the pellet fill weight, not by changing the functional membrane thickness. Compliance for this dosage form is anchored to USP <711> Apparatus I or II with multiple dissolution time points, USP <905> for content uniformity, 21 CFR 211.110 for in-process control, and ICH Q1A(R2) for photostability and formal stability. The API addition ratio in the drug-layering step is 4–8% w/w solids in purified water during Wurster spraying onto 600–710 µm sugar spheres; the functional polymer coating, applied as an aqueous ethylcellulose dispersion with dibutyl sebacate at 10–20% w/w of polymer solids, is built to 12–25% w/w pellet weight gain. In a Wurster bottom-spray chamber of appropriate production scale, inlet air is held at 55–65°C, product temperature at 29–32°C, atomizing air pressure at 1.5–2.0 bar, and spray rate at 5–8 g/min/kg of pellets; partition height is adjusted to 1.5–2.0 times the static bed height to prevent pellet agglomeration and uneven coating. After coating, pellets are dried in a tray dryer at 40°C for 12 h to reduce residual moisture below 2.0% w/w, then lubricated with 0.2–0.3% w/w talc and filled on a dosator capsule filler with fill weight control by in-line weight sorting. Terminal finished dosage forms are extended-release capsules for once-daily oral administration. Dissolution acceptance is set as 20–40% released at 2 h, 50–70% at 6 h, and not less than 80% at 12 h in a two-stage medium of 0.1 N HCl for the first 2 h followed by phosphate buffer at pH 6.8, adapted from USP <711>. Operational boundary: pellets above 2.0% w/w residual moisture during curing cause ethylcellulose film sticking, while coating weight gain below 10% w/w creates a risk of dose dumping on the 2 h dissolution time point.
| Process variable | Operating range | Measurement or control point |
|---|---|---|
| Product temperature | 29–32°C | IR sensor in Wurster chamber |
| Inlet air temperature | 55–65°C | Inlet air probe after heater |
| Coating weight gain | 12–25% w/w | Pellet mass balance before and after coating |
In a 1000 L stainless steel batching vessel with bottom-entry stirrer, the 2 mg/mL memantine hydrochloride oral solution is prepared by dissolving the API in purified water at 20–25°C under continuous mixing, then adding sodium benzoate at 0.1–0.2% w/v, sorbitol solution as a non-cariogenic sweetener, and a citrate buffer system to maintain pH 5.0–6.5; the finished concentration corresponds to 10 mg/5 mL. Compliance for this scenario is governed by USP <51> antimicrobial effectiveness testing, USP <791> pH measurement, 21 CFR 211.113(b) for written procedures, 21 CFR 211.166 for stability, and ICH Q1A(R2) plus ICH Q1B for photostability evaluation. The process sequence includes a 30 min mixing step after pH adjustment, a clarifying filtration through a 10 µm polypropylene cartridge to remove undissolved particulate matter, and filling into 150 mL amber polyethylene terephthalate bottles with child-resistant closures and an oral dosing syringe; the amber packaging is selected because memantine hydrochloride in aqueous solution is assigned a light-protection requirement under the stability protocol. Terminal finished product types are oral solution units at 10 mg/5 mL. Operational boundary: the solution pH is not raised above 7.0, because reduced ionization of the primary amine salt can precipitate memantine base; long-term storage is controlled at 25±2°C and 60±5% RH, with preservative efficacy re-tested at the end of the proposed shelf life per USP <51>.
Bulk granules and unit-dose sachets for memantine hydrochloride are prepared by fluid-bed top-spray granulation rather than direct compression when the target dosage form must be sprinkled on soft food or dispersed in water for patients with swallowing difficulty. The API fraction in the granule formulation is 2.0% w/w for a 5 mg/250 mg sachet fill and 4.0% w/w for a 10 mg/250 mg sachet fill, with mannitol, low-substituted hydroxypropyl cellulose, crospovidone, and a non-reducing sweetener forming the excipient base. Compliance is maintained under 21 CFR 211.84 for component testing, 21 CFR 211.110 for in-process granule moisture and sieve analysis, USP <905> for weight variation of the filled sachet, and ICH Q3D for elemental impurity control. During processing, a 5% w/w hydroxypropyl cellulose binder solution is sprayed onto the fluidized powder bed at inlet air 65–75°C, product temperature 30–35°C, atomizing air pressure 1.5–2.0 bar, and spray rate 10–15 g/min/kg; granulation continues until the granule moisture reaches 1.0–2.0% w/w, followed by sieving through a 1.25 mm mesh and filling by volumetric auger filler into stick packs. Terminal finished product types are unit-dose stick packs and bulk granules in HDPE containers with desiccant. Because the memantine molecule contains a primary amine, reducing sugars such as lactose and glucose are excluded from the aqueous granulation formula to limit Maillard adduct formation; if lactose is unavoidable in a customer formulation, the process is confined to direct compression under low moisture and low heat rather than wet granulation.
Although injectable memantine hydrochloride is not a registered commercial dosage form in the USP-NF or Ph. Eur. and published data for this specific configuration are limited, hospital or clinical trial supply can require a sterile solution prepared from pharma-grade API under an investigational medicinal product framework. For such aseptic manufacture, compliance is derived from EU GMP Annex 1, 21 CFR 210/211 where the product is manufactured as an investigational drug product, USP <1> for injections, USP <85> for bacterial endotoxins, USP <790> for visible particulates, USP <71> for sterility, and ICH Q3D for elemental impurities. The addition ratio is typically proposed as 2 mg/mL memantine HCl in Water for Injection, with sodium chloride at 9 mg/mL to adjust osmolality to 280–320 mOsmol/kg and 0.1 N HCl or 0.1 N NaOH used for pH adjustment to 5.0–6.5. The solution is prepared at 20–25°C, sterile-filtered through a 0.22 µm polyvinylidene fluoride membrane, and filled into sterile Type I glass vials under Grade A/B conditions; terminal sterilization by steam at 121°C for 15 min is not introduced unless pH-specific degradation and impurity profiling have been validated, because published high-temperature degradation data for memantine HCl injection are insufficient to support a default terminal heat cycle. Terminal finished product types are sterile injectable vials intended for intravenous or intramuscular administration within a clinical trial or hospital pharmacy supply chain. Operational boundary: bacterial endotoxin testing per USP <85> must use a product-specific limit calculated from the maximum bolus dose and route of administration, and visible particulate inspection per USP <790> is performed on 100% of filled units before release.
When incoming memantine hydrochloride API exhibits a particle-size distribution with D90 above 150 µm and direct compression fails the content uniformity acceptance limits of USP <905>, high-shear wet granulation is introduced for 5 mg tablet cores. The active addition ratio is 2.5% w/w for a 5 mg/200 mg core, with intragranular mannitol, microcrystalline cellulose, and croscarmellose sodium providing disintegration capacity. Compliance requirements are 21 CFR 211.68 for granulator, mill, and fluid-bed dryer qualification, 21 CFR 211.110 for in-process moisture and granule size monitoring, and ICH Q3C where aqueous binder is used without organic solvents. In a 25 L high-shear mixer, the dry preblend is mixed for 5 min at impeller 200–300 rpm and chopper 1500–2500 rpm; a 5% w/w hydroxypropyl cellulose binder solution is added at 30–40 g/min, with wet massing continued for 90–120 s until the torque signal reaches 8–12 Nm. The wet mass is discharged, milled through a 10 mm screen, dried in a fluid-bed dryer at inlet 65–70°C and product temperature 35–40°C to a final moisture of 1.5–2.5% w/w, then milled through a 0.8 mm screen at 1200 rpm and lubricated with 0.5–0.75% w/w magnesium stearate for 3 min. Compression at 8–12 kN on a rotary tablet press yields 70–90 N tablet hardness, disintegration not more than 10 min per USP <701>, and dissolution testing per USP <711> in 0.1 N HCl. Terminal finished product types are immediate-release 5 mg film-coated tablets, with the same granulation platform extended to 10 mg cores by increasing the granule mass per tablet rather than altering the granulating fluid composition. Operational boundary: the wet massing interval must be closely controlled because overwetting above 120 s produces dense granules that resist disintegration, while underwetting below 90 s leaves unmixed API-rich fines at the mill discharge and increases content uniformity failures.
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For tablet, capsule, granule, and injectable formulation development, memantine hydrochloride pharma-grade API—sometimes transcribed as menantine hydrochloride—is supplied as a white or almost white crystalline powder corresponding to 3,5-dimethyl-1-aminoadamantane hydrochloride, CAS 41100-52-1, molecular formula C12H21N·HCl, and molecular weight 215.76 g/mol. No universal model designation applies; commercial grades are delineated by intended route as oral solid dosage grade and parenteral grade, with route-specific release profiles for particle size, microbial quality, and elemental impurities. The API is released under ICH Q7 GMP conditions with a Type II drug master file or CEP and is specified by the Ph. Eur. and USP monographs for memantine hydrochloride. Representative batch release includes assay by HPLC with an acceptance criterion of 98.0–102.0% on the dried basis, related substances controlled under ICH Q3A thresholds of 0.05% reporting, 0.10% identification, and 0.15% qualification for a daily dose of ≤2 g, loss on drying ≤0.5% by USP <731>, residue on ignition ≤0.1% by USP <281>, residual solvents per ICH Q3C and USP <467>, and elemental impurities per ICH Q3D and USP <232>/<233>. The compound is an uncompetitive NMDA receptor antagonist used in moderate-to-severe Alzheimer disease; finished oral dosage units commonly contain 5–20 mg memantine hydrochloride. Unlike donepezil hydrochloride, galantamine hydrobromide, or rivastigmine, memantine hydrochloride is not an acetylcholinesterase inhibitor and is not directly interchangeable with those agents. Compared with the free base, the hydrochloride salt provides a freely water-soluble crystalline intermediate with reproducible stoichiometry and dissolution behavior. Memantine is achiral; therefore enantiomeric purity is not a release criterion. The oral grade is intended for immediate-release tablets, capsules, and granules; the injectable grade is intended for small-volume parenteral solutions where filtration and endotoxin control are mandatory.
The hydrochloride salt form provides a crystalline, freely water-soluble material with a defined stoichiometric chloride content. Memantine free base exhibits a calculated pKa of 10.27, indicating protonation in the gastric environment; however, salt formation is selected to avoid handling of the neutral amine and to improve blending, dissolution, and batch-to-batch reproducibility. Pharmacopeial solubility classification lists the hydrochloride as freely soluble in water, whereas the free base has lower aqueous solubility. The salt also supports aqueous parenteral compounding without the need for organic co-solvents. Specification of chloride content and assay on the dried basis confirms salt stoichiometry; this distinguishes the pharmaceutical grade from research-grade memantine hydrochloride, which may not be released under ICH Q7 or accompanied by a valid CEP/DMF. The salt form is compatible with direct compression, wet granulation, and extrusion-spheronization processes, provided that the particle size distribution is controlled. Dissolution testing of finished dosage forms is performed by USP <711> using compendial media appropriate for the immediate-release formulation.
Pharmacological differences from other anti-dementia products are material to formulation and clinical use. Memantine hydrochloride is an uncompetitive NMDA receptor antagonist, whereas donepezil hydrochloride and galantamine hydrobromide are acetylcholinesterase inhibitors and rivastigmine is a carbamate inhibitor. This mechanistic distinction means memantine hydrochloride is not titrated on the same cholinergic adverse-effect scale and is not typically associated with cholinergic gastrointestinal effects. For the pharmaceutical manufacturer, the difference matters because memantine hydrochloride API is not interchangeable with those agents in fixed-dose combination tablets; separate compatibility and dissolution testing is required. Unlike rivastigmine, which is chiral, memantine is achiral, so chiral method validation is not required. The oral and injectable grades of memantine hydrochloride therefore differ from other Alzheimer disease APIs both in pharmacology and in release specification requirements.
When memantine hydrochloride is processed into tablet, capsule, and granule dosage forms, particle size distribution and bulk density influence content uniformity, segregation tendency, and downstream flow. In low-dose tablet manufacture, the API is generally pre-blended by geometric dilution or co-milled with microcrystalline cellulose. Production-scale experience on rotary tablet presses indicates that blends with a D90 above 250 µm can segregate in the press hopper, raising content uniformity RSD beyond 3%; lots with D50 between 25 µm and 75 µm and Hausner ratio ≤1.25 are more suitable for direct compression. For wet high-shear granulation in a 600 L bowl granulator, memantine hydrochloride can be added dry or dissolved in the granulating fluid; the solution addition route often improves low-dose distribution but changes granule growth and requires binder adjustment. Capsule filling on dosator and dosing-disc equipment benefits from controlled bulk and tapped density, determined by USP <616>. Granules for oral administration may be prepared by fluid-bed granulation or extrusion-spheronization; the API can partially dissolve during aqueous granulation, so the formulator must verify that recrystallization during drying does not create coarse agglomerates that slow dissolution. Tableted and encapsulated products are tested for dissolution using USP <711> and for blend uniformity using USP <905>.
| Parameter | Oral solid grade | Injectable grade | Method or standard |
|---|---|---|---|
| Appearance | White or almost white crystalline powder | White or almost white crystalline powder | Ph. Eur. 2.2.1, USP <631> |
| Assay on dried basis | 98.0–102.0% | 98.0–102.0% | HPLC, USP <621> |
| Related substances | ICH Q3A reporting 0.05%, identification 0.10%, qualification 0.15% | Same thresholds; route-specific toxicology review | HPLC, USP <621> |
| Loss on drying | ≤0.5% representative | ≤0.5% representative | USP <731> |
| Residue on ignition | ≤0.1% representative | ≤0.1% representative | USP <281> |
| Residual solvents | ICH Q3C Class 1/2/3 limits | ICH Q3C Class 1/2/3 limits | USP <467>, Ph. Eur. 2.4.24 |
| Elemental impurities | ICH Q3D oral PDEs via risk assessment | ICH Q3D parenteral PDEs via risk assessment | USP <232>/<233> |
| Particle size | D90 frequently ≤250 µm; D50 25–75 µm | Solution formulations use dissolved API; powder-for-reconstitution grades may require D90 ≤20 µm | USP <786>, laser diffraction |
| Bulk/tapped density | Report value; Hausner ratio ≤1.25 for direct compression | Not specification-critical for solution products | USP <616> |
| Bacterial endotoxins | Not a release criterion for oral API | Parenteral limit derived from finished-product dose; test required | Ph. Eur. 2.6.14, USP <85> |
| Particulate matter | Not applicable | Finished solution must meet limits after filtration | USP <788> |
| Microbial quality | Non-sterile limits as appropriate | Low bioburden for sterile filtration | USP <61>/<62> |
Batch-to-batch control is maintained by monitoring crystallization parameters, residual solvent profile, and particle size. In oral solid dosage forms, particle size is often more variable than chemical purity; changes in milling configuration or crystallizer shear can shift the D50 by 10–20 µm and alter capsule fill weight or tablet hardness. This is why pharmaceutical grade API is released against route-specific particle size specifications and placed on a control chart during commercial supply. For injectable grade, clean-room handling and low bioburden manufacturing are necessary, and any change in the final crystallization solvent is evaluated under ICH Q3C and ICH Q3D risk assessments. The API manufacturer’s stability data, validation batch records, and analytical method validation reports form part of the regulatory dossier.
Injectable-grade material is differentiated from oral-grade material by the application of bacterial endotoxin, bioburden, particulate matter, and parenteral elemental impurity controls. The API is not necessarily supplied sterile; the final injectable solution is typically sterilized by filtration through a 0.22 µm membrane filter. Therefore, the API must present a low bioburden and endotoxin profile that allows the finished product to meet its validated limit. Endotoxin testing is conducted by Ph. Eur. 2.6.14 or USP <85>; the limit is derived from the maximum bolus dose and the threshold pyrogenic dose, not from a single universal API specification. A 20 mg memantine dose administered to a 70 kg adult yields a relatively high allowable endotoxin limit by USP <85> calculation, but finished-product manufacturers often adopt stricter internal limits to address batch-to-batch variation and excipient contribution. Injectable formulations generally use memantine hydrochloride dissolved in Water for Injection, with tonicity adjustment and pH control; because the API is in solution, laser diffraction particle size is less relevant than clarity, filter compatibility, and insoluble particulate burden. If the API is supplied as a sterile powder for reconstitution, particle size and reconstitution time become critical, and D90 values ≤20 µm are frequently requested. Elemental impurities are assessed using parenteral PDEs from ICH Q3D and USP <232>/<233>. Residual solvent limits follow ICH Q3C, with special attention to any solvent used in the final crystallization step.
Direct compression is selected when the API and excipients demonstrate adequate flow and compressibility without granulation. In memantine hydrochloride low-dose formulations, direct compression often requires a narrow particle size distribution because the API is present at unit loads of 5–20 mg and segregation can produce subpotent or superpotent tablets. A D50 between 25 µm and 75 µm and a D90 ≤250 µm are typical targets for oral solid dosage forms, but these values are not compendial limits; they are qualified through process validation and blend uniformity studies using USP <905>. When the API is too coarse, it may remain in the tablet press feed frame and cause assay drift during long runs. When the API is micronized too aggressively, electrostatic charging can reduce flow and increase sticking to punches. In such cases, the formulator may use a 0.5–1.0% colloidal silicon dioxide glidant, and the API may be pre-screened through a 60-mesh sieve. Compaction properties are assessed by compressibility, compactability, and tabletability studies on an instrumented rotary press; ejection force and punch adhesion are monitored because memantine hydrochloride formulations at high compression force can exhibit lamination if the blend is overlubricated with magnesium stearate above 1.5%. These processing boundaries are specific to the finished formulation and are not defined by the API monograph.
Bulk memantine hydrochloride should be stored in sealed, low-moisture-barrier packaging; double polyethylene bags inside an aluminum foil laminate or HDPE drum are common. In high-humidity regions, opened containers may show an increase in loss on drying if exposed for extended periods, so sampling should be performed under controlled relative humidity. Long-term storage conditions are assigned according to ICH Q1A(R2) or WHO stability guidance for the relevant climate zone; a retest period is established from real-time data, with accelerated testing at 40°C/75% RH and intermediate testing at 30°C/65% RH where applicable. Solid-state degradation is generally slow; the main stability concerns are moisture uptake and the formation of related substances under thermal stress. In aqueous injectable formulations, pH control, trace metal management, and oxygen exclusion may be required because solution-state degradation can differ from solid-state behavior. The API is not regarded as highly hygroscopic, but packaging and handling should prevent surface moisture accumulation in humid environments. No antioxidant or chelator is required solely for the API; excipient compatibility studies determine the final formulation stability. The product should be protected from strong oxidizing agents and incompatible excipients in the dry state. Data on degradation kinetics in compounded memantine hydrochloride solutions is limited; therefore compatibility with infusion fluids should be confirmed before use.