| HS Code | 880315 |
| Product Name | L-Arginine alpha-Ketoglutarate (1:1) |
| Synonyms | AAKG; Arginine AKG; L-Arginine ketoglutarate |
| Cas Number | 16856-18-1 |
| Molecular Formula | C11H20N4O7 |
| Molecular Weight | 320.30 g/mol |
| Appearance | White or almost white crystalline powder |
| Odor | Slight characteristic odor |
| Solubility | Freely soluble in water; sparingly soluble in ethanol |
| Melting Point | Approximately 220 °C with decomposition |
| Ph 1 Aqueous Solution | 6.0 - 8.0 |
| Assay Content | 98.0% - 102.0% on dried basis |
| Storage Conditions | Store in a well-closed container in a cool, dry, and well-ventilated place |
| Shelf Life | 24 months when stored properly |
As an accredited L-arginine alpha ketoglutarate (1:1) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | L-arginine alpha-ketoglutarate (1:1) is supplied in a sealed foil pouch containing 500 g white powder, labeled with batch and expiry. |
| Container Loading (20′ FCL) | 20′ FCL loading of L-arginine alpha ketoglutarate (1:1) ensures secure, efficient transport, maximizing payload while preserving product quality and safety. |
| Shipping | L-arginine alpha-ketoglutarate (1:1) ships as a non-hazardous, non-DG powder. Pack in sealed, moisture-resistant inner bags inside sturdy fiber drums or cartons. Protect from heat, humidity, and direct sunlight. Transport at ambient temperature in clean, dry containers. Ensure labels and documentation accurately identify the chemical and comply with all applicable regulations. |
| Storage | Store L-arginine alpha-ketoglutarate (1:1) in a tightly sealed container in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, and excessive moisture. Keep away from incompatible substances. Use within the manufacturer’s expiration date. No special refrigeration is typically required if stored under recommended conditions. |
| Shelf Life | Shelf life is typically 2 years when stored in a cool, dry place, protected from moisture and heat. |
Production dry blending of L-arginine alpha-ketoglutarate (1:1) is governed by the salt’s hygroscopicity, which makes ambient relative humidity the dominant environmental variable. In a double-ribbon blender operating at 12–15 RPM with a vessel fill volume of 55–65%, a homogeneous mix is typically reached within 12–18 min when the blend room is held below 40% RH. The loading sequence places colloidal silicon dioxide at the bottom of the vessel, followed by AAKG, and then lower-density flavour systems, creatine monohydrate, and electrolyte salts, so that fine light particles do not stratify under high-shear convective mixing. Blend uniformity is verified by sampling at 10 production-scale locations and analysing all active and marker components by HPLC with acceptance criteria aligned to USP <905>; acceptance values above 15 trigger a documented out-of-specification investigation under 21 CFR 111.70. The free moisture content of the finished powder is controlled between 0.8% and 1.5% by Karl Fischer titration according to USP <921> because excursions above 2.0% in this matrix increase interparticle bridging and cause the powder to compact inside the filling auger. Finished sachets or tubs are packed with a desiccant in foil-lined polyethylene terephthalate laminate film, and the line is cleared every 4 h to remove residual hygroscopic build-up from contact surfaces. Published data for the exact hold-time threshold under production-scale conditions for this specific 1:1 salt are limited, so manufacturer-specific deviation histories should be used to refine the 40% RH set point.
High-shear wet granulation of AAKG-containing tablet formulations requires substitution of an aqueous binder with 95% ethanol or anhydrous isopropyl alcohol because the 1:1 salt dissolves readily in water, leading to over-wetted masses, uncontrolled granule growth, and drying room bottlenecks. A vertical high-shear granulator with a 10 L bowl, impeller tip speed 4–6 m/s, and chopper speed 1500 RPM is commonly used for pilot-scale production, with liquid addition over 90–120 s and wet massing not exceeding 180 s. The wet granules are discharged through a 0.8 mm screen and dried in a fluid-bed dryer with inlet air temperature 40–50°C and dew point not higher than -10°C, until loss on drying reaches 1.0–2.0%. Dried granules are dry-milled, blended with 1.0% w/w magnesium stearate for 3 min, and compressed on a rotary tablet press with a main compression force adjusted to produce tablet hardness between 70 N and 120 N for an 8 mm concave tooling set. Coated tablets are evaluated for friability according to USP <1216> with a maximum weight loss of 1.0%, disintegration according to USP <701> with a limit of 30 min in purified water, and content uniformity according to USP <905>. The terminal dosage form is a moisture-barrier film-coated tablet, typically using an HPMC/PVA coating system, which reduces surface tackiness and protects the core from ambient humidity during bulk storage.
| Process route | Critical variable | Control window | Reference method |
|---|---|---|---|
| Dry powder blend | Blend room relative humidity | ≤40% | NIST-traceable hygrometer |
| Dry powder blend | Free moisture | 0.8–1.5% | USP <921> |
| Wet granulation | Inlet air dew point | ≤-10°C | Chilled mirror hygrometer |
| Wet granulation | Loss on drying | 1.0–2.0% | Forced-air moisture balance |
| Tablet compression | Breaking force | 70–120 N | USP <1217> |
| Capsule filling | Fill weight RSD | ≤3.0% | In-process balance check |
When encapsulation room ambient relative humidity exceeds 45%, AAKG powder begins to adhere to tamping pin surfaces and dosator tubes, producing fill weight relative standard deviations above 3.0% and intermittent machine faults. The preferred equipment is an intermittent-motion capsule filler configured for size 00 hydroxypropyl methylcellulose or gelatin capsules, with a forced feeder maintaining a constant hopper level and a line speed typically reduced to 70–80% of maximum to limit frictional heat. Before filling, the blend is conditioned to a moisture content below 1.5% by Karl Fischer titration, and flowability is improved with 0.5–1.5% colloidal silicon dioxide plus 0.5–1.0% magnesium stearate, mixed in a bin blender at 12 RPM for 10 min. Powder flow is characterised using the angle of repose method under USP <1174>; values above 40° are considered marginal for high-speed encapsulation and may require dry granulation instead of simple blending. In-process fill weight checks are performed every 15 min with a mass balance, and the encapsulation suite is held at 20–25°C so that condensation risk at the powder surface remains low. Finished capsules are placed in amber high-density polyethylene bottles with a desiccant canister and an induction seal; if the product is marketed as a dietary supplement, components and finished batches are managed under 21 CFR 111.70 and 21 CFR 111.75. Long hold times above 8 h between blending and capsule sealing are not recommended because the salt’s moisture uptake increases fill weight variation and may initiate surface dissolution at the capsule wall.
In neutral-pH ready-to-drink amino acid beverages, the addition of AAKG at 1.5–3.0 g per 500 mL depresses pH in a buffer-dependent manner and must be neutralised with potassium citrate or sodium bicarbonate before thermal processing. The liquid batch is prepared by pre-dissolving AAKG in treated water at 15–25°C under a high-shear disperser, then adding non-reducing sweeteners such as sucralose or acesulfame potassium because the primary amine of arginine participates in Maillard browning when heated with reducing sugars. The pH is adjusted to the target specified for hot-fill stability, commonly between 3.5 and 4.0, with pH measured by USP <791>, and the solution is processed through a plate heat exchanger at 95°C for 30 s before hot filling at 85°C into polyethylene terephthalate bottles. Dissolved oxygen is controlled below 0.5 mg/L by nitrogen sparging to limit oxidative by-product formation during shelf life. The terminal product is a single-serve RTD amino acid beverage, but published data for the exact stability of AAKG in this specific configuration are limited, and real-time shelf-life testing under 25°C/60% RH is required to confirm label claim retention over 12 months. If the formulation contains fermentable carbohydrate sources, the manufacturer must also validate pasteurisation efficacy under ISO 22000:2018 Clause 8.5.1 rather than relying solely on pH as a food safety barrier.
Single-serve sachet lines for clinical oral nutrition require tighter environmental control than conventional sports supplements because the product may be consumed by metabolically stressed populations. AAKG is dry-blended with maltodextrin, electrolytes, and water-soluble vitamins in a low-bioburden suite with EU GMP Grade D equivalent air classification, and the contact surfaces are sanitised with 70% isopropyl alcohol before each campaign. The raw material specification includes loss on drying not more than 1.5%, heavy metals by ICP-MS not more than 10 ppm lead and 5 ppm arsenic, and microbial enumeration according to USP <61> with total aerobic count not exceeding 10³ CFU/g, yeast/mould not exceeding 10² CFU/g, and absence of Escherichia coli and Salmonella in 10 g according to USP <62>. The blend is filled into foil-laminate sachets under nitrogen flush to maintain headspace oxygen below 2%, and fill weight variation is controlled to ±2% of target by a servo-driven auger filler. The terminal product is an oral nutritional powder that is dispersed in water before consumption, with label formatting under 21 CFR 101.9. The main operational boundary is that AAKG cannot be steam sterilised in finished-powder form, so microbial control must be achieved through ingredient specification and environmental controls rather than terminal sterilisation.
A 5 g serving of the anhydrous 1:1 salt delivers 2.72 g L-arginine and 2.28 g α-ketoglutarate by stoichiometric mass balance, based on the molecular weights 174.2 g/mol and 146.1 g/mol for the two components. In multi-ingredient pre-workout powders that also contain citrulline, beta-alanine, taurine, caffeine, and electrolytes, the large differences in particle size and bulk density between AAKG and low-dose actives create segregation during blending and filling. To correct this, the low-dose actives are pre-dispersed through a 0.25 mm screen and then combined with AAKG in a low-shear tumble blender for 20 min, after which a high-intensity shear step is avoided so that the crystalline structure of AAKG is not fractured into fines. If segregation potential remains unacceptable, the formulation is dry granulated by roll compaction at roll pressure 4–6 MPa, milled to 0.8 mm, and then blended with a hydrophobic flow aid. The finished powder is filled into stick packs with target fill weight 10–15 g and maximum fill weight RSD 1.5% across a 10 000-pack campaign. Certificate of analysis testing for each batch includes identity by Fourier transform infrared spectroscopy, assay by HPLC, moisture by USP <921>, and blending uniformity by USP <905>. The main incompatibility is with aqueous liquid transport: once AAKG is dissolved, it should not be held with reducing sugars or heated above 80°C for prolonged periods because arginine accelerates browning and α-ketoglutarate degradation may reduce measured assay values.
Competitive L-arginine alpha ketoglutarate (1:1) prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
L-arginine alpha ketoglutarate (1:1) is the equimolar salt of L-arginine and alpha-ketoglutaric acid. The product is identified as CAS 16856-18-1 and may be represented by the formula C6H14N4O2·C5H6O5, giving a calculated molecular weight of 320.30 g/mol. The calculated L-arginine mass fraction is 54.4%, with the remaining 45.6% contributed by alpha-ketoglutaric acid. This distinction matters for label claims because the alpha-ketoglutarate portion contributes to the total formula weight but is not L-arginine. The salt is typically supplied as a white to off-white crystalline powder, a densified direct-compression granulate, or a micronized powder. Supplier model designations for these forms are not harmonized across compendial standards; the certificate of analysis should therefore state particle-size method, loss on drying, assay method, and the exact counterion mass used for calculation. Because no USP, Ph.Eur., or FCC monograph is specific to the 1:1 salt, release testing is based on supplier specifications and general chapters such as USP <731> for loss on drying, USP <281> for residue on ignition, and USP <232> / <233> or ICH Q3D for elemental impurities. The material is generally sold for dietary supplement solid oral dosage forms and is not to be assumed sterile or suitable for parenteral use without additional controls.
Model designations should always specify the 1:1 stoichiometry because L-arginine alpha ketoglutarate can also be offered as a 2:1 salt in some supplier catalogs. The 2:1 material contains two moles of L-arginine per mole of alpha-ketoglutaric acid, giving a higher calculated L-arginine mass fraction and different handling properties. In procurement records, the term “AAKG” is ambiguous unless the stoichiometric ratio is attached. Standard crystalline powder, densified direct-compression granulate, and micronized grade are all sold under supplier-specific model names; the direct-compression grade is not merely a finer powder but a granule designed for tablet feed-frame flow.
In dry powder blending, the selection between L-arginine salts is often based on calculated L-arginine mass fraction, chloride load, and hygroscopicity. AAKG 1:1 has a calculated L-arginine mass fraction of 54.4%, while L-arginine hydrochloride has 82.7% and L-arginine base has 100.0%. L-citrulline is not an arginine salt and contributes 0.0% arginine by mass, although it is used as a metabolic precursor in dietary supplement formulations. The replacement factor for L-arginine HCl to AAKG 1:1 is 1.52 when maintaining equivalent calculated L-arginine mass; the replacement factor for L-arginine base to AAKG 1:1 is 1.84. These conversion factors are arithmetic and do not establish equivalent clinical response, because dissolution rate, solution pH, and absorption cannot be inferred from mass fraction alone.
| Ingredient | CAS | Molecular weight (g/mol) | Calculated L-arginine mass fraction (%) | Salt stoichiometry |
|---|---|---|---|---|
| L-Arginine alpha ketoglutarate (1:1) | 16856-18-1 | 320.30 | 54.4 | 1:1 L-arginine:alpha-ketoglutaric acid |
| L-Arginine hydrochloride | 1119-34-2 | 210.66 | 82.7 | 1:1 L-arginine:HCl |
| L-Arginine base | 74-79-3 | 174.20 | 100.0 | None |
| L-Citrulline | 372-75-8 | 175.19 | 0.0; arginine metabolic precursor | None |
The chloride-free nature of AAKG 1:1 may be relevant when a formulation already contains potassium chloride or sodium chloride for electrolyte fortification, where additional chloride from L-arginine HCl can affect the total mineral load. In contrast, L-arginine HCl is often specified when a simple, less hygroscopic crystalline salt is desired and the chloride counterion is acceptable. The alpha-ketoglutarate component of AAKG 1:1 also contributes titratable acid equivalents and can chelate polyvalent metal ions in solution, which is not observed with L-arginine HCl or L-arginine base. Published equilibrium and stability data for the 1:1 salt in multicomponent premixes are limited; therefore, forced degradation and compatibility testing under controlled temperature and humidity are required before a commercial blend is locked.
Methods for incoming identification often include FTIR and powder X-ray diffraction. The 1:1 salt shows characteristic carboxylate bands from alpha-ketoglutarate that are absent in L-arginine HCl and L-arginine base. Ion chromatography can confirm the absence of chloride in AAKG 1:1; this is useful when a producer is replacing L-arginine HCl and needs to verify the final mineral load. X-ray powder diffraction distinguishes the crystalline forms because the 1:1 salt has its own lattice parameters and is not a physical mixture of L-arginine and alpha-ketoglutaric acid. Reference diffractograms should be requested from the supplier and retained for change control.
In a production-scale dry blending sequence, AAKG 1:1 is usually charged after a portion of the diluent has been pre-blended with fumed silica. The sequence reduces electrostatic wall adhesion in stainless-steel V-blenders and bin blenders. Blenders are commonly run at 10 to 15 rpm for 15 to 20 minutes; the required time to blend uniformity is established by sampling and assay under a validated protocol rather than by fixed rule. At relative humidity above 60%, the powder surface begins to absorb water, and caking can occur if the headspace is not conditioned. Pre-drying in a fluid-bed dryer with inlet air at 40°C until loss on drying falls below 1.0% is a common corrective action. Direct-compression premixes often contain 0.5 to 2.0 wt% fumed silica or calcium silicate; flow-aid levels above 2.0 wt% can produce hydrophobic regions that slow tablet disintegration under USP <701>. The moisture content after blending should be verified by Karl Fischer titration or USP <921> Method 1a because ambient humidity during transfer can reverse the drying step.
Particle-size distribution affects segregation in multi-ingredient premixes. A coarse standard powder with D90 above 200 µm can segregate from finely milled flavoring or sweetener components during bin discharge; a micronized grade improves suspension uniformity but increases dust exposure. Sieve analysis is performed under USP <786> or ISO 2591-1, and the acceptance band is set to the mixer type and transfer distance. For direct-compression feeding, the densified model is generally used because it reduces bridging in the hopper and maintains die fill consistency.
Direct compression of AAKG 1:1 requires a densified supplier model because un-milled crystalline powder can exhibit poor flow and low bulk density in high-speed feed frames. A rotary tablet press with pre-compression is typically used; the pre-compression force is set at approximately 20% of the main compression force to remove air and reduce lamination. Target tablet hardness is usually 6 to 8 kp for standard round tooling, and friability is monitored according to USP <1216> with a maximum of 1.0%. Weight variation is evaluated under USP <905>. Tablet press speed must be adjusted to the granulation flow; high shear in the feed frame can create fines that change ejection force and increase the risk of picking or sticking to upper punches. Compression zones should be maintained at relative humidity below 60% because the salt can hydrate at the tablet surface if the powders are stored in open hoppers.
For capsule filling, a dosator or tamping-style machine may require different fill density adjustments than crystalline L-arginine HCl. The bulk and tapped densities of AAKG 1:1 are reported on the supplier certificate under USP <616>; these values change with residual moisture and particle-size distribution. Capsule blends are often pre-sieved through a 0.8 mm screen to break agglomerates before filling. However, published comparative tableting data for AAKG 1:1 in a standardized excipient matrix remain limited, so the compression and ejection parameters are developed experimentally for each supplier grade. Dissolution or disintegration of the finished dosage form is evaluated under USP <711> or USP <2040> as appropriate for the label claim.
Raw material release testing for AAKG 1:1 usually includes identification, assay, water content, residue on ignition, elemental impurities, and residual solvents. Because the salt is a stoichiometric adduct, assay results should state whether the method quantifies intact salt, L-arginine content, or alpha-ketoglutaric acid content. A non-aqueous titration may measure only the basic L-arginine component; HPLC with UV or charged aerosol detection can separate the alpha-ketoglutarate anion. When assay is expressed as intact salt on dried basis, the supplier limit is commonly 98.0% to 102.0%. If the assay is expressed as L-arginine, the specification must be adjusted to the calculated 54.4% mass fraction and verified with a reference method.
| Property | Method reference | Typical criterion |
|---|---|---|
| Appearance | Visual | White to off-white crystalline powder |
| Identification | FTIR vs. reference; HPLC retention time | Corresponds to standard |
| Assay, dried basis | HPLC or non-aqueous titration | 98.0%–102.0% |
| Loss on drying | USP <731> | Not more than 1.0% or supplier-dried basis |
| Residue on ignition | USP <281> | Not more than 0.1% |
| Elemental impurities | USP <232>/<233>; ICH Q3D Option 1 | Complies for oral solid dosage materials |
| Residual solvents | USP <467> | Complies with relevant class limits |
| Bulk/tapped density | USP <616> | Reported for lot-to-lot compression control |
These release controls are not a demonstration of product efficacy or clinical performance. They define the quality of the raw material entering the mixing operation. If the material is intended for sterile or preserved aqueous dosing, additional bioburden, endotoxin, and preservative efficacy testing are required; standard dietary supplement grades are not manufactured under aseptic conditions. In the United States, finished dietary supplement manufacturing is subject to 21 CFR Part 111, and product labels must comply with 21 CFR 101.36 where applicable. Suppliers should provide REACH registration or equivalent for EU use and confirm that the material is not classified under CLP. For food additive applications outside dietary supplements, regulatory status should be verified separately because the salt may not be listed for general food use in all jurisdictions.
The main bulk-storage boundary is moisture control. Packaged AAKG 1:1 should be stored in a dry area at or below 25°C with relative humidity below 60%. Once a drum is opened, the remaining product should be re-sealed under dry nitrogen or placed in a dessicant-lined container because the powder can absorb atmospheric water within a single shift. Aqueous stock solutions should be prepared at 20°C to 25°C and used within the working day unless a preservative system and pH control are validated. The alpha-ketoglutarate moiety can chelate polyvalent metal ions, so prolonged contact with unlined carbon steel is avoided; 316L stainless steel or high-density polyethylene equipment is preferred. The salt should not be dry-mixed with strong oxidizing agents, strong acids, or aldehydes. With reducing sugars under heated drying, carbonyl–amine condensation can generate brown Maillard-type products and reduce available arginine. Thermal stress above 40°C during drying should be avoided unless forced degradation data demonstrate stability, because the alpha-keto acid component may be sensitive to prolonged heating. Hot water or steam washdown is not recommended for spilled powder; dry vacuum recovery with a HEPA-filtered collector is used to prevent creating a wet alkaline film on equipment.
For dietary supplement powder formulations, AAKG 1:1 is added at the mass fraction required to deliver a target calculated L-arginine equivalent. A dosage form designed to contain 3.0 g of L-arginine base would require 5.52 g of AAKG 1:1 if the conversion factor 1.84 is used. The equivalent L-arginine HCl input would be 3.63 g. These calculations are for mass balance only and do not imply interchangeable absorption or physiological effect. If the 2:1 salt is accidentally purchased and treated as 1:1, the delivered arginine mass will be overestimated; sample identification should include the stoichiometric ratio and preferably FTIR reference authentication. Published data comparing the salt with other arginine sources in the same finished matrix remain limited, so formulators should not extrapolate from single-dose studies without matrix-specific compatibility data.