| HS Code | 295070 |
| Productname | Nicotinamide Mononucleotide Pharma Grade API |
| Synonyms | NMN; β-Nicotinamide Mononucleotide; Nicotinamide Ribotide |
| Casnumber | 1094-61-7 |
| Molecularformula | C11H15N2O8P |
| Molecularweight | 334.22 g/mol |
| Appearance | White to off-white crystalline powder |
| Purity | ≥99.0% (HPLC) |
| Grade | Pharma Grade API |
| Dosageforms | Tablet, Capsule, Granule, Injection |
| Routesofadministration | Oral, Injectable |
| Solubility | Soluble in water |
| Storageconditions | Store at -20°C for long term or 2-8°C short term, protected from light and moisture |
| Shelflife | 24 months when stored under recommended conditions |
| Packaging | Aluminum foil bag, pharmaceutical drum, or sterile vial for injection |
| Qualitystandard | Manufactured under GMP; complies with pharmaceutical API requirements |
| Sterility | Sterile grade available for injectable use |
| Endotoxin | Controlled for injectable grade |
As an accredited Nicotinamide Mononucleotide 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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Direct compression of NMN into tablet cores begins with delumping the API through a conical mill fitted with a 0.610 mm screen at 1,000–2,000 rpm to break agglomerates without generating excessive sub-10 µm fines. The milled API is blended with microcrystalline cellulose, crospovidone, colloidal silicon dioxide, and sodium stearyl fumarate in a two-stage bin blender sequence: an initial 5 min pre-blend of NMN with colloidal silicon dioxide and half the filler, followed by a 12 min final blend. Tablets are compressed on a rotary tablet press using precompression force of 6–10 kN and main compression force of 18–25 kN, producing cores with 6–10 kp hardness and friability below 1.0% w/w per USP <1216>. Formulation addition ratios range from 30–70% w/w NMN. A 250 mg NMN tablet core at 600 mg total weight uses 41.7% w/w NMN, 48.5% w/w microcrystalline cellulose, 4.0% w/w crospovidone, 0.5% w/w colloidal silicon dioxide, and 1.5% w/w sodium stearyl fumarate. The API-to-filler ratio is held at 1:0.5 to 1:2.0 to prevent segregation and content uniformity drift. Release testing follows ICH Q7 and 21 CFR Part 211.110; blend uniformity and assay use an ICH Q2(R1)-validated HPLC method, and finished tablets are tested for content uniformity per USP <905>, dissolution per USP <711>, and friability per USP <1216>. The process window narrows when ambient relative humidity exceeds 40% RH; if loss-on-drying of the blend exceeds 2.0% w/w, pre-drying in a fluid-bed dryer at 40°C for 2 h is applied to restore flow and prevent punch sticking. Terminal product types include direct-compressed film-coated tablets, scored tablets, and biconvex round cores in 6–12 mm diameters.
| Finished dosage form | Primary GMP and regulatory standard | Compendial finished product test standard | Process-control reference |
|---|---|---|---|
| Tablet | 21 CFR Part 211, ICH Q7 | USP <711>, USP <905>, USP <1216> | USP <616>, USP <1174> |
| Capsule | 21 CFR Part 211, ICH Q7 | USP <711>, USP <905> | USP <616>, USP <786> |
| Granule | 21 CFR Part 211, ICH Q7 | USP <711>, USP <905>, USP <786> | USP <616> |
| Lyophilized injection | EU GMP Annex 1, 21 CFR Part 210, 21 CFR Part 211 | USP <1>, USP <71>, USP <85>, USP <788>, USP <790>, USP <1207> | ISO 13408-1, ISO 14644-1 |
| Liquid injection | EU GMP Annex 1, 21 CFR Part 210, 21 CFR Part 211 | USP <1>, USP <71>, USP <85>, USP <788>, USP <790>, USP <1207> | ISO 13408-1, ISO 14644-1, USP <1663>, USP <1664> |
For NMN hard-shell capsule filling, the hygroscopic API is pre-sifted through a 0.800 mm sieve and premixed with colloidal silicon dioxide before being loaded into the encapsulator hopper. Direct-fill operations on a tamping pin or dosator machine are run at 15–25 N plug compression force with pin diameters between 14 mm and 18 mm to create plugs that remain intact during transfer but disintegrate rapidly after shell rupture. Capsule content weight control is maintained at ±3.0% during filling; when fill-weight drift exceeds this band, the blend is re-assayed and the dosing station is reset. A typical formulation addition ratio uses 125 mg, 150 mg, or 250 mg NMN per capsule, with NMN comprising 20–50% w/w of the total fill weight, microcrystalline cellulose 35–65% w/w, croscarmellose sodium 2–5% w/w, sodium stearyl fumarate 0.5–1.0% w/w, and colloidal silicon dioxide 0.5–1.0% w/w. The API-to-diluent ratio is held between 1:0.75 and 1:3.0 to accommodate the low bulk density of milled NMN and the limited capsule volume. During process validation, capsule contents are tested for uniformity of dosage units per USP <905>, dissolution per USP <711>, and moisture content by Karl Fischer titration; in-process checks follow 21 CFR Part 211.110 and ICH Q7. Completed capsules are stored with desiccant canisters because a humid API fill can transfer moisture to the shell, causing brittleness or dimensional deformation. Terminal product types include HPMC two-piece capsules, pullulan capsules, and enteric-coated capsules where subsequent modified release is required. Published stability data for the enteric-coated NMN capsule configuration are limited; before adopting an enteric film, forced degradation and acid-stage dissolution data must be generated for the specific shell and coating system.
At sachet fill weights below 1.5 g, fluid-bed granulation of NMN into directly soluble or swallowable granules is used to improve powder flow and reduce dusting during high-speed vertical form-fill-seal operations. NMN is dry blended with mannitol, xylitol, or erythritol and granulated in a top-spray fluid bed using a binder solution of povidone K30 or hypromellose 3 cps at 3–8% w/w dry binder level. Spray rate is maintained at 20–40 g/min, inlet air temperature at 55–70°C, product temperature at 28–35°C, and atomization air pressure at 1.5–2.5 bar. Drying is continued until loss-on-drying reaches 1.5–3.0% w/w; the dried granulate is milled through a 0.8 mm screen and blended with 0.5% w/w colloidal silicon dioxide before packaging. Formulation addition ratio for a 100 mg NMN sachet uses NMN 8–25% w/w of the finished granule blend, filler 50–80% w/w, binder 3–8% w/w, sweetener or flavor 0.5–2.0% w/w, and anti-caking agent 0.5–1.0% w/w. Release testing includes particle size distribution per USP <786>, bulk density and tapped density per USP <616>, uniformity of dosage units per USP <905>, and dissolution per USP <711>. In effervescent systems, citric acid and sodium bicarbonate are kept separate from NMN until final dry blending because the acidic environment may accelerate degradation; published NMN effervescent compatibility data are limited, and a forced degradation matrix should be run under ICH Q1A(R2) before commercial formulation. Terminal product types include stick-pack granules, sachet granules, and effervescent granules sealed in aluminum foil laminate with low moisture vapor transmission rate.
Injectable-grade NMN for lyophilized vials is dissolved in Water for Injection at 20–100 mg/mL, with mannitol added at 2–10% w/v as a crystalline bulking agent that supports cake structure. The solution pH is adjusted to 6.5–7.4 with dilute sodium hydroxide or hydrochloric acid; phosphate or citrate buffer strength is limited to 10–50 mM to avoid buffer salt crystallization during freezing. Fill solution is aseptically filtered through a 0.22 µm PVDF membrane and filled into 5 mL or 10 mL Type I glass vials at 2–5 mL fill volume in an ISO 5 environment. Vials are partially stoppered with bromobutyl rubber closures, loaded onto freeze-dryer shelves pre-chilled to 2–8°C, frozen to -40°C at a cooling rate of 0.5°C/min, held for 2–4 h, then primary dried at -10°C to -20°C at chamber pressure 80–150 mTorr for 24–72 h. Secondary drying is conducted at 25°C for 6–12 h to reduce residual moisture to below 1.0% w/w. Formulation addition ratio uses 50–200 mg NMN per vial with a mannitol-to-NMN mass ratio of 1:1 to 2:1. The freeze-dried product is tested for appearance, reconstitution time, residual moisture by Karl Fischer, sub-visible particulate matter per USP <788>, visible particulates per USP <790>, sterility per USP <71>, and bacterial endotoxins per USP <85>; container closure integrity is verified by USP <1207>. Compliance with EU GMP Annex 1, ISO 13408-1, ISO 14644-1, and 21 CFR Part 211.167 is required for the sterile filling and lyophilization line. Terminal product types include lyophilized cake in Type I glass vials with bromobutyl stoppers; reconstitution with Sterile Water for Injection yields a solution for injection, but in-use stability must be validated for the specific dose and container.
Because published data on terminal steam sterilization of NMN in aqueous solution are limited, liquid injectable manufacturing is designed around aseptic filtration rather than terminal heat treatment. The bulk solution is prepared at 10–50 mg/mL NMN in Water for Injection, with sodium chloride 0.9% w/v for isotonicity, and the pH is adjusted to 6.0–7.4 using dilute hydrochloric acid or sodium hydroxide. Buffer salts, when used, are limited to 10–25 mM to avoid hypertonicity and potential precipitation. Filter compatibility testing is performed on polyethersulfone and polyvinylidene fluoride membranes with 0.22 µm pore size; filtration pressure is maintained below 14 psi to reduce particle shedding and membrane fouling. Fill volume ranges from 1 mL to 20 mL depending on container choice. The solution is filled in an ISO 5 environment using peristaltic pumps and sterile single-use tubing; headspace is flushed with nitrogen to limit oxidative degradation. In-process hold time between final filtration and filling is validated to avoid more than 4 h at 15–25°C, unless supported by solution stability data. The finished product is tested for visible and sub-visible particulates per USP <790> and USP <788>, bacterial endotoxins per USP <85>, sterility per USP <71>, and container closure integrity per USP <1207>. Extractables and leachables are assessed according to USP <1663> and USP <1664> for the selected rubber stopper, plunger, or ampoule glass type. Compliance requirements include EU GMP Annex 1, ISO 13408-1, ISO 14644-1, and 21 CFR Part 210 and 21 CFR Part 211. Terminal product types include single-dose vials, ampoules, and pre-filled syringes in Type I glass or cyclic olefin polymer containers with low-oxygen permeation.
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Nicotinamide Mononucleotide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a β-nicotinamide mononucleotide active substance supplied as a white to off-white crystalline powder. The CAS registry number is 1094-61-7, the molecular formula is C11H15N2O8P, and the anhydrous molecular mass is 334.22 g/mol. The product is not a finished dosage form; it is an active pharmaceutical ingredient whose grade model is selected according to the intended dosage-form process and route of administration. Product models are segregated by intended route and processing path rather than by chemical identity: oral direct-compression grade, capsule-grade powder, granule-grade powder, and injectable-grade low-endotoxin powder. Each grade differs principally in residual water, bioburden, endotoxin, and particle-size acceptance criteria; the underlying molecular structure is unchanged.
Representative release limits for commercial NMN API are summarised in the following table. These values are drawn from typical certificate-of-analysis parameters; because no harmonised pharmacopoeial monograph is published for nicotinamide mononucleotide, the method designator is aligned with the applicable general chapter.
| Parameter | Method designator | Oral tablet/capsule/granule grade | Injectable grade |
|---|---|---|---|
| Appearance | Visual | White to off-white crystalline powder | White to off-white crystalline powder |
| Assay, anhydrous basis | USP <621> | 98.5–101.5% | 98.0–101.5% |
| β-anomer purity | USP <621> | ≥99.0% | ≥99.0% |
| Water content | USP <921> | ≤1.0% | ≤0.5% |
| Bacterial endotoxins | USP <85> | Not routinely specified | ≤0.25 EU/mg |
| Sterility | USP <71> | Not required | Passes if labelled sterile |
| Total aerobic microbial count | USP <61> | ≤100 CFU/g | ≤10 CFU/g |
| Total yeast and mould count | USP <61> | ≤10 CFU/g | ≤1 CFU/g |
| Residual solvents | USP <467> | ICH Q3C Option 1 | ICH Q3C Option 1 |
| Elemental impurities | ICH Q3D | Risk assessment based | Risk assessment based |
For oral solid dosage forms, the assay is normalised on the anhydrous, solvent-free basis; loss on drying is not used as a substitute for Karl Fischer water determination because surface moisture and hydrate water can differ. HPLC methods commonly use a reversed-phase column with dimensions of 250 mm × 4.6 mm packed with 5 µm C18 silica, detection at 254 nm, and an isocratic mobile phase comprising phosphate buffer and methanol. The β-anomer peak is integrated against a working standard of known purity. Total impurities are controlled with a reporting threshold of 0.05 area% and an identification threshold of 0.10 area%, following ICH Q3A principles. For injectable use, endotoxin testing is added and a pre-filtration bioburden limit of ≤10 CFU/100 mL is applied to the bulk solution before sterilising filtration.
Processing of oral solid dosage forms with NMN is dominated by the hygroscopic phosphate-ester structure and the need to control moisture below the point at which the powder loses compressibility. Bulk and tapped densities are measured according to USP <616>; a Hausner ratio above 1.35 indicates the need for roller compaction or wet granulation before tablet compression. Direct-compression grade NMN is typically pre-blended with colloidal silicon dioxide at 0.5–1.0 wt% and sodium stearyl fumarate at 0.5–1.5 wt%; magnesium stearate may be used but over-lubrication above 2.0 wt% can reduce tablet tensile strength. On a rotary tablet press fitted with 10.0 mm round B-tooling, feed-frame speed is maintained between 20–40 rpm and compression force is adjusted to achieve a target hardness of 60–100 N for tablets with a mass of 300 mg. The finished tablet must meet disintegration not more than 15 min in purified water at 37.0 °C per USP <701> and dissolution not less than 80% in 30 min using USP <711> Apparatus 2 at 50 rpm in 900 mL water. For capsules, a dosator-type capsule filler with size 0 capsules is used; the tamping-pin station is adjusted to produce a target fill weight tolerance of ±5%. The low bulk density of untreated NMN powder can require densification by slugging or dry granulation before encapsulation; if the as-received poured density is below 0.30 g/mL, the flowability may not support weight uniformity at production speeds above 60,000 capsules/h.
For granule-grade NMN intended for sachets or suspension, high-shear or fluid-bed granulation is employed. In a high-shear mixer, purified water is added at 10–20 wt% of dry powder mass; impeller tip speed is held between 5–10 m/s and chopper speed between 1500–3000 rpm for 3–6 min to reach a median granule size of 150–250 µm by laser diffraction per USP <429>. The wet mass is transferred immediately to a fluid-bed dryer; inlet air temperature is limited to 40–50 °C to avoid solution-phase hydrolysis. The final granule moisture is confirmed below 1.0% by Karl Fischer titration before terminal blending. If the granules are to be filled into stick packs, the final blend is passed through a 1.0 mm conical screen and the moisture is checked again at the fill-line hopper.
Injectable administration requires the API to be free of bacterial endotoxins and to meet particle-count limits that are irrelevant for tablets or capsules. For NMN injectable grade, the bacterial endotoxin limit is ≤0.25 EU/mg by kinetic chromogenic LAL per USP <85>, and the bulk solution is filtered through a 0.22 µm polyethersulfone sterilising-grade filter before aseptic filling. The filling line is operated in an ISO 5 unidirectional airflow environment defined by ISO 14644-1, with glove-box or restricted-access-barrier systems used to reduce human intervention; this is consistent with EU GMP Annex 1. Terminal sterilisation is avoided for NMN unless the formulation is shown to survive moist heat; published data for this specific configuration is limited. After filling, each container is inspected for visible particles per USP <790>. For subvisible particles, the light-obscuration method of USP <787> is used; limits for small-volume injections are ≤6000 particles ≥10 µm and ≤600 particles ≥25 µm per container. The injectable grade also has a residual moisture limit of ≤0.5% because free moisture can promote hydrolysis and may alter the lyophilisation cake or solution clarity. pH adjustment is performed after complete dissolution with 0.1 N HCl or NaOH to a target of 6.0–7.0; the product is not a buffered solution unless a specific buffer salt is added, and the use of phosphate buffer must be evaluated for compatibility with calcium-containing infusion fluids.
The principal product difference between NMN and other nicotinamide-based NAD-precursor ingredients is the presence of the phosphate group on the ribose. Nicotinamide riboside chloride has a molecular mass of 290.70 g/mol and is a cationic molecule at acidic formulation pH, whereas NMN is dianionic at neutral pH; this changes its interaction with croscarmellose sodium, sodium starch glycolate, and methacrylic acid copolymers. Nicotinamide itself has a molecular mass of 122.12 g/mol, is uncharged, and is far less hygroscopic; it can be wet-granulated without the same degree of moisture sensitivity. From a purification standpoint, NMN contains a β-glycosidic bond and a phosphate ester; the main process-related impurities include the α-anomer, nicotinamide, ribose phosphate, and residual solvents. In oral tablet formulations, the α-anomer is controlled at not more than 1.0–2.0% because it may not be biologically equivalent; HPLC method capability rather than pharmacopoeial specification currently governs this limit. Injectable NMN differs from oral NMN in that the injectable grade cannot be simply an oral powder that has been sterilised; the incoming API must already have low bioburden and low endotoxin because terminal filtration does not remove soluble endotoxin.
The behavior of NMN in water determines the critical handling limits in both granulation and injectable preparation. In water, the phosphate group dissociates and can reduce the pH of an unbuffered solution; a 1.0% w/v aqueous solution may fall in the acidic range, and the exact value depends on residual counterion content. The solution is therefore pH-adjusted rather than simply hydrated. For wet granulation, a 10–20 wt% water level is used to avoid a continuous free-water phase; the addition rate is set so that the wet mass reaches a target loss-on-drying of 8–12% before entering the dryer. The granules are then screened through a 1.0 mm screen and dried to ≤1.0% moisture. In injectable compounding, dissolved oxygen is reduced by nitrogen sparging to below 0.5 mg/L, and the solution is held at 2–8 °C for not more than 24 h before sterile filtration to limit hydrolysis; this hold-time is based on general aseptic processing practice because published forced-degradation data for NMN under these exact conditions is limited. The use of phosphate-buffered vehicle is evaluated for precipitation risk; calcium-containing diluents should be avoided because the phosphate group can form insoluble calcium phosphate complexes.
Packaging for oral tablet/capsule/granule grade uses double low-density polyethylene liners sealed in aluminium foil laminate with a desiccant; storage is at 15–25 °C and ≤35% RH. The injectable grade is supplied in Type I glass vials with bromobutyl stoppers, stored at 2–8 °C and protected from light. The material is re-tested every 24 months for oral grade and every 12 months for injectable grade under ICH Q1A(R2)-compliant stability protocols. For shipment, temperature excursion below 0 °C is permitted for injectable grade only if moisture ingress is prevented, while oral grade does not require cold-chain transport. Published data for this specific configuration is limited.
Release and formulation activities are referenced to the following standards and guidance documents. The absence of a specific NMN monograph in USP, Ph. Eur., or JP means that the listed general chapters are applied as scientifically appropriate rather than as compendial requirements for the molecule.
| Standard or guidance | Function |
|---|---|
| USP <621> | Chromatographic purity, assay, and β-anomer determination |
| USP <921> | Water content by Karl Fischer titration |
| USP <85> | Bacterial endotoxins |
| USP <71> | Sterility of injectable finished product |
| USP <790> / USP <787> | Visible and subvisible particle control |
| ICH Q3D | Elemental impurities |
| USP <467> | Residual solvents |
| USP <61> / USP <62> | Microbial enumeration and specified organism control |
| 21 CFR 211 | CGMP finished pharmaceutical and API operations |
| ISO 14644-1 | Cleanroom classification for aseptic filling |