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Monosodium Glutamate

    Specifications
    HS Code 245290
    Chemical Name Monosodium glutamate
    Molecular Formula C5H8NNaO4
    Molecular Weight 169.11 g/mol
    Cas Number 142-47-2
    E Number E621
    Appearance White crystalline powder
    Solubility Soluble in water, slightly soluble in ethanol
    Taste Umami taste of savory meat-like flavor
    Ph 6.0 - 8.0 (0.5% aqueous solution at 25°C)
    Melting Point 232°C (decomposes)
    Density 1.635 g/cm³ at 20°C
    Production Method Fermentation of carbohydrates using Corynebacterium glutamicum
    Storage Conditions Store in a cool, dry, well-ventilated area, keep container tightly closed

    As an accredited Monosodium Glutamate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Monosodium glutamate is packaged in a sealed 500 g plastic pouch with a safety label and resealable closure.
    Container Loading (20′ FCL) Monosodium glutamate in 25 kg bags, loaded into a 20′ FCL container, approximately 27 tons, secured properly.
    Shipping Monosodium glutamate ships as a non-hazardous food additive in sealed, food-grade packaging to prevent moisture absorption and contamination. Keep containers dry, ventilated, and away from strong odors. Ensure labeling meets food safety regulations. Avoid extreme temperatures. Handle with standard hygiene protocols to maintain product purity and quality.
    Storage Store monosodium glutamate in an airtight container in a cool, dry place away from direct sunlight, heat, and moisture. Keep it tightly sealed when not in use to prevent caking and absorption of odors. Under these conditions, MSG remains stable and retains its flavor for an extended period.
    Shelf Life Monosodium glutamate has a shelf life of about 2 years when stored in a cool, dry place, retaining flavor.
    Application of Monosodium Glutamate

    In dry-mix operations for compressed bouillon cubes and granular savoury compounds, monosodium glutamate monohydrate is pre-blended with sodium chloride, hydrogenated vegetable fat, sucrose, and native starch in a horizontal ribbon blender operated at 12–18 rpm for 6–10 min; this residence time is sufficient for a coefficient of variation below 5% only when the mixer fill does not exceed 80% of working volume. The E621 fraction with a mean sieve cut of 0.10–0.40 mm segregates from coarse salt crystals of 0.60–1.40 mm when the batch is discharged through the bottom gate at high flow rates, so drop height after discharge is limited to 500 mm and intermediate surge hoppers are fitted with inclined baffles. Dry bouillon premixes typically incorporate E621 at 5–15 wt% of the dry non-fat portion, with the precise level determined by the desired glutamate-to-sodium ratio in the finished cube. The premix is compacted between counter-rotating rollers at 30–50 kN linear force, milled to a free-flowing granulate with 0.8–1.5 wt% residual moisture, and pressed into cubes on a rotary tablet press; cube surface cracking becomes visible when the granulate fraction above 1.0 mm exceeds 5% of batch mass because oversize particles disrupt the packing density at the die wall. Finished cubes are conditioned to a water activity below 0.55 before foil wrapping to prevent glutamate caking during pallet storage. Regulatory classification for this application derives from Codex STAN 192-1995 Table 3, where INS 621 is permitted under conditions of good manufacturing practice, from Annex II to Regulation (EC) No 1333/2008 for E 621 in dry soups and bouillon bases, and from 21 CFR 182.1 as a generally recognised as safe multipurpose food substance in the United States. Terminal product types include hard bouillon cubes, granular bouillon, powdered seasoning blends, and compressed seasoning tablets. The dominant production-scale failure mode is not chemical degradation but physical segregation: vertical sampling across the ribbon blender trough after 10 min of mixing frequently shows a glutamate-enriched lower stratum when the sodium chloride fraction contains more than 20% particles retained on a 0.80 mm sieve.

    Why Does E621 Solubility Govern Pre-Blend Uniformity in Spray-Dried Soup Bases?

    In spray-dried soup base production, monosodium glutamate monohydrate is added to the aqueous phase before high-shear dispersion; its dissolution rate in multi-solute slurries drops substantially when sodium chloride, maltodextrin DE 10–15, and hydrolysed vegetable protein compete for free water. The dry powder formula contains E621 at 5–10 wt%, and it is pre-dissolved in a jacketed mixing tank at 55–65°C before combining with heat-labile starch and oil fractions. The slurry is homogenised through a 150 µm screen and pasteurised in a plate heat exchanger at 85°C for 15 s, then dried in a co-current spray dryer with a rotary atomiser operated at 18,000–22,000 rpm, inlet air at 180–200°C, and outlet air at 85–95°C; incomplete dissolution before the homogeniser leaves fine glutamate crystals that act as nucleation sites in the atomiser, producing dryer bearding, a drop in bulk density from 0.35–0.45 g/mL to below 0.30 g/mL, and an increase in fines below 100 µm. Post-dryer fluidised-bed agglomeration at 55–65°C with lecithin as binder restores instant solubility and reduces dust. Packaging lines for the resulting powder specify a moisture vapour transmission rate no greater than 0.5 g/m²/24 h at 38°C and 90% RH when tested according to ASTM F1249, and the package headspace oxygen is held below 2% to retard lipid oxidation in the soup base. Regulatory coverage is provided by Codex STAN 192-1995 Table 3 for dry soup mixes, by Regulation (EC) No 1333/2008 Annex II where E 621 is authorised quantum satis in soups, and by 21 CFR 182.1 in the United States. Terminal products include dry soup mixes, instant noodle flavour sachets, powdered gravy bases, and dehydrated sauce mixtures. The most common production bottleneck occurs in the solubilisation tank: a 5,000 L batch containing 250–500 kg E621 at 15°C may require 20–30 min with a low-shear propeller agitator, whereas a high-shear rotor-stator reduces complete dissolution to 8–12 min and lowers the defect rate from undissolved particles in the dryer.

    During high-speed comminution of mammalian and avian trimmings, monosodium glutamate is introduced after initial salt-soluble myofibrillar protein extraction but before fat emulsification, because early addition of high-ionic-strength glutamates can depress the extractability of salt-soluble proteins if the batter temperature is outside the 4–6°C window. In emulsified sausage batters, E621 addition levels are maintained between 0.20% and 0.35% of raw batter mass; these levels are effective only when disodium 5′-ribonucleotides are present at approximately 5–10% of the E621 mass, creating a glutamate-nucleotide umami potentiation that allows sodium reductions of 10–20% in the final formulation. The E621 is added in the second stage of a vacuum bowl chopper at 2,000–3,600 rpm under −0.8 bar vacuum after 40–60% of the chopping cycle, when the lean-phase batter has reached 4–6°C; this delayed addition prevents early crystalline dissolution and preserves protein–protein gelation during subsequent thermal processing. In injection-brined poultry, E621 is dissolved in the chilled brine at 0.10–0.25% of green meat weight and injected through multi-needle arrays at 1.5–2.0 bar; in ground meat patties it is mixed into the coarse-ground lean phase at 0.15–0.30% of mass before final grinding. Regulatory oversight for meat systems is governed by Regulation (EC) No 1333/2008 Annex II category 8.2.1 for processed meat, by Codex STAN 192-1995 for relevant meat product categories, and by 21 CFR 182.1 in the United States. Terminal products include frankfurters, bologna, mortadella, injection-brined poultry rolls, beef patties, and frozen meatballs.

    E621 addition level and insertion point across comminuted meat systems
    Meat systemTypical addition levelProduction insertion pointTerminal product types
    Emulsified sausage batter0.20–0.35% of raw batter massSecond-stage vacuum bowl chopper after 40–60% of cycle at 4–6°CFrankfurters, bologna
    Injection brine0.10–0.25% of green meat weightDissolved in chilled brine before multi-needle injection at 1.5–2.0 barPoultry rolls, ham analogues
    Ground meat patties0.15–0.30% of massMixed into coarse-ground lean phase before final grindBeef patties, frozen meatballs

    When Savoury Snack Seasoning Requires Electrostatic Adhesion Control on Low-Moisture Extrudates

    On low-moisture extruded snack lines, topical seasoning adhesion is governed by the mean particle diameter of the dust, the oil film on the snack base, and the residence time in the rotary coating drum. For topical seasoning blends, monosodium glutamate is milled to a mean particle diameter of 75–150 µm; the blend contains 5–12 wt% E621 and is dosed at 3–8 wt% of the extrudate mass through a loss-in-weight screw feeder into a baffled coating drum rotating at 6–10 rpm. The drum is fitted with electrostatic discharge monitoring because the friction of fine glutamate particles against stainless steel baffles can generate static potentials above 25 kV, producing uneven deposition and increased dust extraction. Immediately before the dusting station, a heated vegetable-oil spray system applies 2.5–5.0% oil by mass at 40–50°C; oil below 2.0% produces dust fall-off during downstream vibratory conveying, while oil above 6.0% causes the seasoning powder to agglomerate at the feeder screw. Under these conditions the finished snack carries 0.20–0.80 g E621 per 100 g of finished product, and the glutamate remains stable because the frying or baking surface temperature of 160–180°C is below the onset of thermal decomposition at 232°C. Regulatory frameworks for savoury snacks include Codex STAN 192-1995 Table 3, Regulation (EC) No 1333/2008 Annex II for E 621 in savoury snack categories, and 21 CFR 182.1 in the United States. Terminal product classes include extruded corn curls, potato crisps, coated nuts, and pellet-fried snack products. The recurring production failure occurs in humid environments: when ambient air exceeds 65% RH, glutamate crystals partially dissolve on the oily snack surface, producing translucent patches and increasing bag-to-bag seasoning loss after 30 days of ambient storage.

    Because the moromi phase of brewed soy sauce fermentation already contains endogenous L-glutamic acid released by Aspergillus oryzae proteolysis, exogenous E621 is not introduced until after raw shoyu has been pressed, clarified, and pasteurised in a plate-type steriliser at 85–90°C for 15–30 s. In post-fermentation liquid condiment compounding, E621 is metered into a blending tank equipped with a bottom-mounted agitator operating at 250–500 rpm, with the addition level limited to 0.20–0.60% w/v of the final product because the fermented base already contributes 0.30–1.60 g/100 mL free glutamate depending on moromi age and temperature history. If E621 is added before pasteurisation, residual reducing sugars in the condiment can drive Maillard and transamination side reactions at elevated temperature, reducing analytically quantifiable glutamate and increasing absorbance at 430 nm beyond specification; post-pasteurisation addition avoids this pathway. The finished condiment is cooled to 20–25°C before final filtration through a 0.45 µm membrane and aseptic filling into glass or HDPE bottles. Compliance for liquid condiments is based on Codex STAN 192-1995 Table 3, where INS 621 is permitted under good manufacturing practice in fermented sauces, and on Regulation (EC) No 1333/2008 Annex II for E 621 in liquid seasonings; manufacturers targeting North American markets rely on 21 CFR 182.1 GRAS status, while exports to China fall under GB 2760 Table A.2 as a permitted flavour enhancer. Terminal finished products include amino-acid-enriched soy sauce, ponzu, teriyaki-type liquid seasoning, hydrolysed vegetable protein sauces, and concentrated dip bases. The significant process condition is not shear or thermal input but tank hygiene: residual quantities of sodium chloride at 18–20% in the base condiment can form localised brine pockets in low-speed mixing zones, delaying E621 dissolution until the final holding phase and causing variability in finished-product titration values.

    Cryogenic Freeze–Thaw Stability of E621 in Frozen Meal Sauce Systems

    Monosodium glutamate partition behaviour under freeze–thaw cycling is governed by the unfrozen water phase concentration around ice crystal boundaries, not by initial mixing concentration alone. In cook-chill and cook-freeze production, monosodium glutamate is incorporated at 0.15–0.45% of the sauce mass during the final 10–15 min of kettle cooking, after modified waxy maize starch has reached peak viscosity; this sequencing prevents the low-molecular-mass glutamate from competing with starch granules for available water earlier in the hydration curve. The sauce is filled into multi-layer barrier trays at 65–70°C, passed through a spiral freezer to reach −18°C core temperature within 90 min, and stored at −23°C during distribution. During freeze–thaw cycling, E621 partitions into the unfrozen water fraction and can reach local concentrations up to three times the bulk formulation in the ice-crystal boundaries, but precipitation does not occur because the solubility limit of the monohydrate at −1°C remains above 60 g/100 mL. Microwave reheating in 800–1,000 W ovens creates local temperature gradients of 10–15°C across the sauce mass; the low molecular weight of E621 (169.11 g/mol) ensures rapid re-equilibration during reheating and prevents the delayed umami release that is otherwise observed with encapsulated seasonings. Regulatory classification for prepared meals follows Codex STAN 192-1995 Table 3 and Regulation (EC) No 1333/2008 Annex II, where E 621 is authorised quantum satis in composite meal categories, while 21 CFR 182.1 covers use in the United States; national sodium-reduction front-of-pack targets rather than food additive law impose the practical upper bound. Terminal finished products include frozen lasagna, butter chicken sauce portions, macaroni cheese meal bases, and tray-sealed microwaveable entrées with sauce components. The principal production-scale defect is not E621 degradation but re-crystallisation at the tray surface when the sauce is held above 0°C for more than 2 h before blast freezing; this surface film becomes visible as white specks after reheating and is mitigated by top-surface oil spray at 0.5–1.0% of sauce mass prior to tray sealing.

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    Certification & Compliance
    More Introduction

    Monosodium L-glutamate is supplied as the sodium salt of L-glutamic acid, with the anhydrous form assigned CAS 142-47-2 and the crystalline monohydrate assigned CAS 6106-04-3. The monohydrate, C₅H₈NNaO₄·H₂O, has a molecular weight of 187.13 g/mol; the anhydrous form has 169.11 g/mol. Industrial manufacture proceeds by aerobic fermentation of starch hydrolysates or cane molasses with Corynebacterium glutamicum, followed by neutralisation with sodium hydroxide, decolourisation, crystallisation, and drying. Food-grade material appears as white, practically odourless crystals or crystalline powder and is freely soluble in water, with an approximate solubility of 74 g/100 mL at 25 °C. A solution of 5 g/100 mL has pH 6.7–7.2. The substance is identified as E621 under Regulation (EC) No 1333/2008 and as a generally recognised as safe food substance under 21 CFR 182.1. Two physical models are traded in dry blending: the monohydrate crystal for general seasoning and the anhydrous powder for low-moisture dry mixes where water of crystallisation must be minimised.

    Why Does FCC Assay Require a Dried Basis When the Monohydrate Crystal Is Used?

    Because the monohydrate contains water of crystallisation, a direct weight-basis assay would understate the active C₅H₈NNaO₄ content. The Food Chemicals Codex monograph and the JECFA specification for INS 621 therefore express assay on the dried basis, with a range of 99.0–101.0% as C₅H₈NNaO₄. Specific rotation is controlled at +24.8° to +25.3° as a 10 g/100 mL solution in 2 N HCl at 25 °C, which distinguishes the L-configuration from D-glutamate contaminants. Loss on drying is limited to ≤0.5%, and lead is limited to ≤1 mg/kg. The pH specification of 6.7–7.2 in a 5% solution confirms the mono-sodium stoichiometry; a lower pH would indicate excess glutamic acid, while a higher pH would indicate residual alkali from incomplete neutralisation. This pH window is critical for dry-blend stability because free glutamic acid reduces solubility rate and can alter buffering in subsequent food processing.

    Food Chemicals Codex and JECFA monograph limits for monosodium L-glutamate
    ParameterLimit or typical valueReference method
    Assay, dried basis99.0–101.0% as C₅H₈NNaO₄FCC Monosodium L-Glutamate monograph; JECFA INS 621
    Specific rotation [α]D25+24.8° to +25.3°JECFA, 10 g/100 mL in 2 N HCl
    pH6.7–7.2FCC, 5 g/100 mL aqueous solution
    Loss on drying0.5%FCC, monohydrate
    Lead1 mg/kgFCC
    Solubility in water74 g/100 mL at 25 °CPublished physical data

    Regulatory safety evaluations by JECFA have assigned an acceptable daily intake “not specified” for L-glutamic acid and its sodium salt, indicating that no numerical intake limit was necessary under the conditions of the evaluation. Under EU Regulation (EC) No 1333/2008, E621 is permitted as a food additive in many food categories according to quantum satis; the specific category limits and restrictions are defined in Annex II to that regulation. For pharmaceutical excipient applications, a USP-NF monograph may be applied where the supplier declares the product as pharmacopeial grade; additional limits on microbial load and residual solvents then become batch-release parameters rather than food-grade requirements.

    In liquid soups, gravies, and meat marinades, monosodium glutamate is incorporated at 0.1% to 0.8% by mass of the finished product; in dry seasoning blends, the substance may be combined with salt, spices, and anticaking agents at higher concentrations, but the final meal-level concentration remains below the self-limiting sensory optimum in most matrices. Because the molecule dissociates in the aqueous phase without a holding time, it does not require a thermal reaction step; however, high-shear mixing at temperatures above 80 °C can accelerate Maillard reactions when reducing sugars are present, leading to browning and loss of available glutamate in extended retort cycles. On snack seasoning lines, crystalline MSG is delivered from vibratory feeders into oil-spray tumble drums; adhesion efficiency depends on oil temperature, oil coverage, and the particle size distribution of the seasoning blend. Field experience indicates that fine powder fractions below 80 mesh increase dusting losses and can build up on drum walls, while large crystals above 30 mesh can produce uneven topical distribution. Dehumidified conveying air is used in packaging rooms above 70% relative humidity to prevent surface moisture adsorption and caking on contact surfaces. Published failure-rate data for these specific line configurations is limited.

    In comminuted meat batters, monosodium glutamate is incorporated at 0.2% to 0.6% of total batch mass after the salt-soluble myofibrillar protein extraction step. It contributes perceived savouriness without functioning as a water-activity depressant or a curing agent. Sodium chloride at concentrations below 1.8% in the aqueous phase reduces extraction of myofibrillar proteins; replacement of salt with MSG does not restore this extraction function and can produce a soft or crumbly texture if salt is reduced below the matrix-specific threshold. In cured meat systems, nitrite curing salts remain the preservation system; MSG is added strictly as a flavour potentiator.

    When Ribonucleotide Synergy Changes the Sodium Reduction Calculation

    Disodium 5'-inosinate and disodium 5'-guanylate potentiate the umami response from monosodium glutamate; a common commercial blend is 95:5 MSG to disodium 5'-ribonucleotide, although the exact optimum varies with food matrix and native ribonucleotide content. This interaction permits a reduction in total MSG addition without suppressing perceived savoury intensity. It does not, however, replace the functional roles of sodium chloride in water-activity control, ionic strength, and protein solubilisation. Sodium content is therefore calculated separately for MSG and salt: the monohydrate contributes 12.3 g/100 g sodium, while sodium chloride contributes 39.3 g/100 g. A 1:1 mass replacement of salt with MSG reduces sodium input by 68.7% for the replaced fraction, but practical replacement is limited by saltiness perception and preservation requirements, commonly to 20–30% in neutral-pH soups and ready meals. Sensory evaluation for such reformulation work should follow ISO 8586 assessor-selection principles and ISO 5492 vocabulary definitions when panel data are generated.

    Compositional comparison for dry seasoning ingredients
    IngredientPrincipal componentsSodium contentPrimary sensory functionReference identity
    Monosodium L-glutamate, monohydrateC₅H₈NNaO₄·H₂O, assay 99.0–101.0%12.3 g/100 gUmami, mouthfeel, slight saltinessE621; 21 CFR 182.1
    Sodium chlorideNaCl39.3 g/100 gSaltiness, water-activity reductionFood ingredient
    Yeast extractAmino acids, peptides, nucleotides, cell-wall polysaccharidesMatrix-dependent; supplier specification requiredUmami, bouillon, slight bitter notesFood ingredient
    Hydrolyzed vegetable proteinMixed amino acids, peptides, salt, residual reducing sugarsMatrix-dependent; often elevated by added saltBrothy, meaty, browning potentialFood ingredient

    Unlike hydrolyzed vegetable protein, which contains mixed amino acids, peptides, salt, and reducing sugars, monosodium glutamate is a single molecular entity with defined purity. Hydrolyzed vegetable protein can generate brown colour through Maillard reactions and may introduce bitter or acidic peptide fractions. Yeast extract adds nucleotides and cell-wall glycans that can increase viscosity and contribute a non-neutral taste. Pure MSG provides umami without adding colour or turbidity, and its assay specification allows precise formulation control. Monopotassium L-glutamate is available as an alternative glutamate salt when sodium must be excluded, but it introduces potassium at high substitution rates and may produce a metallic side-taste in neutral matrices. Calcium diglutamate and magnesium glutamate are also used in low-sodium flavour systems, but their solubility and crystal forms differ from the monosodium crystal, and their use is often limited by off-taste and cation-specific functional effects. Published quantitative sensory data comparing all glutamate salts in identical food matrices is limited.

    Granular and Powdered Crystal Habit Constraints in Automatic Dosing Lines

    Commercial monosodium glutamate is distributed in granular, fine, and ultrafine crystal habit grades. Granular material is commonly controlled through sieve fractions such as through 20 mesh to on 60 mesh, while fine powder may be specified through 60 mesh to on 200 mesh; these ranges are supplier-specific and not compendial. Sieve analysis should be performed using test sieves conforming to ISO 3310-1. Bulk density typically falls between 0.80 g/cm³ and 1.00 g/cm³ depending on crystal aspect ratio and moisture content. In automatic dosing systems, fine grades increase cohesive flow hazards; flow function measurements by shear cell according to ASTM D6128 are used to select hopper angle and outlet diameter. On production lines with vibratory feeders, segregation is controlled by matching the feeder tray amplitude to the crystal size distribution; attrition against rotary valve clearances can generate fines that shift the flow regime and increase dust loss. The monohydrate crystal is more resistant to attrition than brittle agglomerated yeast extract powders, but irregular crystal aggregates from high-temperature drying can show batch-to-batch variation in angle of repose. Where the same feeder is used for MSG and salt alternately, line-cleaning protocols are required because salt can absorb surface moisture and accelerate caking of residual MSG on contact surfaces. Published data for specific equipment failure modes with this exact configuration is limited.