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Monosodium Glutamate

    • Product Name: Monosodium Glutamate
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code
    Product Name Monosodium Glutamate
    Chemical Formula C5H8NO4Na
    Molecular Weight 169.11 g/mol
    Cas Number 142-47-2
    E Number E621
    Iupac Name Sodium 2-aminopentanedioate
    Appearance White crystalline powder
    Odor Odorless
    Taste Umami
    Solubility In Water Soluble
    Melting Point 232 °C (decomposes)
    Ph 6.7 to 7.2 (5% solution)
    Density 1.62 g/cm³
    Assay Purity 99.0% to 100.5%
    Moisture Content ≤0.5%
    Sodium Content Approximately 12.3%
    Primary Use Flavor enhancer
    Production Method Fermentation of starch or sugar
    Packaging 25 kg bags, fiber drums, or bulk
    Storage Conditions Cool, dry, well-ventilated area
    Shelf Life 2 years in sealed container
    Hs Code 29224200

    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 Food-grade white crystalline powder packed in a sealed 25 kg multi-wall paper bag with moisture-barrier liner, labeled Monosodium Glutamate for bulk use.
    Container Loading (20′ FCL) 20′ FCL container loaded with Monosodium Glutamate in 25 kg bags, palletized, shrink-wrapped, and safely secured for ocean freight.
    Shipping Monosodium glutamate is generally shipped as a non-hazardous, food-grade commodity. It is packaged in moisture-barrier bags, fiber drums, or bulk containers, kept dry and protected from contamination. Transport by truck, rail, or sea under normal cargo conditions; no special dangerous-goods handling required. Follow local food-safety and customs regulations.
    Storage Store monosodium glutamate at room temperature in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly closed, clearly labeled, and protected from moisture because it is hygroscopic. Segregate from strong oxidizing agents and other incompatible materials. Avoid generating dust, use local exhaust ventilation if needed, and follow the manufacturer’s SDS and local regulations.
    Shelf Life Monosodium glutamate has an indefinite shelf life when stored dry, sealed, and away from moisture; it does not readily spoil.
    Application of Monosodium Glutamate

    In dry bouillon cube and granular compound seasoning manufacture, monosodium glutamate is incorporated as the principal free glutamate carrier while sodium chloride and 5′-ribonucleotides are blended concurrently to establish the umami-to-salty ratio. The incorporation range in pressed bouillon base is 8–18 wt% of the dry mix; in multipurpose culinary seasoning, the range narrows to 3–8 wt%; in spray-dried stock powder, 5–12 wt%. These ranges are not statutory maxima. Codex STAN 192-1995 lists INS 621 as GMP in the relevant soup, broth, and seasoning categories, including food categories 12.2 and 12.5; EU 1333/2008 Annex II Part E authorizes E 621 quantum satis in the same applications, and 21 CFR 182.1 recognizes the substance as GRAS with no numerical limit. The JECFA evaluation assigns an ADI of “not specified.” On the production line, dry blends are charged into a horizontal ribbon mixer at 20–40 m/min tip speed for 6–10 min, with hygroscopic carriers such as maltodextrin and lactose added prior to MSG to reduce contact moisture. Agglomeration in a fluidized-bed unit at 60–80 °C inlet air builds particle density to 0.6–0.9 g/cm³, after which rotary presses compact fat-coated granulates into cubes at 1.3–1.6 g/cm³ cube density. Moisture is held below 2.0%; if ambient RH exceeds 60%, pre-drying of carriers is required because free glutamic acid at the crystal surface absorbs water and initiates caking. Finished goods include hard bouillon cubes, dual-layer soft tablets, granular stock bases, and dry noodle flavoring packets.

    Standard or regulationDesignationApplication condition
    Codex STAN 192-1995INS 621GMP in food categories 12.2, 12.5
    EU 1333/2008 Annex II Part EE 621Quantum satis in processed foods
    21 CFR 182.1Monosodium glutamateGRAS; no numerical limit
    JECFAGlutamateADI not specified

    What Limits Umami Distribution in Topically Seasoned Extruded Snack Lines?

    Topical seasoning of expanded snack pieces imposes the most severe particle-size and adhesion constraints in MSG application because the dry blend is applied after frying or extrusion expansion through a slinger, drum tumbler, or electrostatic belt. In snack dusting powders, MSG is compounded at 2.0–5.0 wt% of the seasoning blend, and the blend is applied at 6–10 wt% of the base snack weight, giving a finished-product free glutamate load of 0.12–0.50 wt%. Regulatory compliance for snack categories falls under Codex STAN 192-1995 INS 621 GMP; EU 1333/2008 allows E 621 quantum satis in the same foods, while US practice is covered by 21 CFR 182.1. Where a sodium reduction claim is used, the reference values of Regulation (EC) No 1924/2006 require at least 25% sodium reduction versus the ordinary product; reformulation cannot be achieved by simple MSG substitution because sodium chloride contributes both ionic strength and bulk adhesion. Production-scale seasoning lines hold fried or expanded pieces at 50–60 °C before oil spraying at 6–12 wt% and dusting in a baffled rotating drum. The free glutamate fraction is screened to 150–250 µm to match salt and sugar particle dimensions; finer grades below 100 µm segregate and produce unstable deposits, while coarser grades above 300 µm create loose salt-like crystals that drop off in packaging. Ambient humidity above 55% in the seasoning room can cause powder bridging at the feeder throat; dehumidification is required before bulk storage. A continuous loss-in-weight feeder controls dusting rate, and an electrostatic applicator is used for low-oil products to reduce dust waste. Terminal product types include fried potato chips, pellet-expanded snacks, corn curls, tortilla chips, coated crackers, and air-popped grains.

    Brine injection and vacuum tumbling of pork, poultry, and emulsified meat products use monosodium glutamate at lower finished concentrations than dry seasonings because the aqueous phase contacts extracted myofibrillar proteins and the injection pump-up ratio determines final retention. Typical brines contain 0.5–1.5 wt% MSG, salt, phosphates, erythorbate, and sometimes starch or carrageenan. At a pump-up of 40–60%, the calculated finished product content is 0.10–0.40 wt%, assuming 85–95% brine retention after cooling. Authorization is governed by EU 1333/2008 for E 621 in heat-treated meat products and marinated preparations; in the United States, 21 CFR 182.1 GRAS applies, and the USDA Food Safety and Inspection Service recognizes the substance in ready-to-eat meat and poultry formulations under approved labeling. In practice, phosphates are dissolved first in cold water to prevent phosphate-salt reaction haze; MSG is added next with sodium chloride to maintain ionic strength. The brine is introduced through multi-needle injectors at 2–4 °C, then the meat is tumbled under vacuum at 0.8–0.9 bar for 4–6 h intermittently to extract salt-soluble myofibrillar proteins. MSG does not interfere with nitrite-curing reactions but should not be preblended with sodium nitrite at high humidity because localized acid condensation can accelerate nitrite oxidation. Finished products include cooked ham, turkey breast rolls, emulsion sausages, marinated raw poultry fillets, and injection-enhanced pork loin.

    When Retort Heating Reduces Free Glutamate Recovery in Ambient Liquid Umami Bases

    Liquid seasoning bases and ambient sauces expose monosodium glutamate to wet heat, reducing sugars, and long residence times; the chief thermodynamic risk is not glutamate decomposition but Maillard-derived loss through reaction with reducing sugar carbonyls at pH above 6.0. Formulations are adjusted to 0.2–0.6 wt% finished-product MSG for general marinades and liquid condiments, and 0.4–0.8 wt% for concentrated ramen soup bases. Compliance is governed by EU 1333/2008 Annex II Part E for E 621 quantum satis, Codex STAN 192-1995 INS 621 GMP, and 21 CFR 182.1 GRAS. In batch production, MSG is dissolved at 55–65 °C before starches and thickeners are dispersed; starch addition after full ionic hydration avoids lumping and local high-viscosity pockets. The liquid is then passed through a tubular or plate heat exchanger for UHT at 135–140 °C for 2–5 s, or filled into retort pouches and processed at 121 °C for 20–30 min. Free glutamate recovery after high-sugar retort conditions can be matrix-dependent; published data for arbitrary commercial soy and tomato sauces is limited, and a controlled in-plant validation using HPLC with o-phthaldialdehyde derivatization is required before increasing retort time. Operational boundaries include avoiding prolonged holding above 70 °C with reducing sugars and pH > 6.5, and adding the MSG component after starch gelatinization when retort browning is unacceptable. Terminal finished products include soy sauce, liquid seasoning, dashi concentrate, retort curry sauce, and teriyaki glaze.

    Chilled and frozen ready-meal systems incorporate monosodium glutamate primarily in sauce and binding components rather than as a dry surface dust because freeze-thaw cycling and microwave reheating redistribute water-soluble flavor compounds toward the container surface. The sauce fraction is formulated at 0.4–0.8 wt% MSG, corresponding to 0.15–0.50 wt% of the assembled meal depending on sauce-to-solid ratio. EU 1333/2008 authorizes E 621 quantum satis in the relevant processed meal categories; Codex STAN 192-1995 and 21 CFR 182.1 apply to international shipments. The industrial sequence consists of kettle cooking at 85–95 °C to a target core temperature of 75 °C, hot filling into barrier trays or pouches, blast chilling to ≤4 °C within 2 h, and freezing to −18 °C. MSG is added after sauce thickening but before final heat-off, so that the ionic environment does not break starch gel networks. Direct dispersion into the hot oil phase is avoided because the crystals do not dissolve and form localized clumps. Terminal frozen and chilled products include assembled beef stroganoff, chicken tikka masala, pasta alfredo, rice bowls, meal kits, and side vegetable coatings.

    High-Moisture Extrusion, Soy Leghemoglobin, and Glutamate Synergy in Meat Analogues

    Plant-based meat manufacturing presents a split-process decision for MSG: pre-extrusion addition survives high shear only partially, while post-extrusion marinade addition achieves more consistent free glutamate concentration but requires a separate liquid injection or tumbling step. In high-moisture extrusion of pea and soy protein concentrates, MSG is generally applied at 0.20–0.50 wt% of the wet extrudate or 0.5–1.0 wt% of a post-extrusion flavor marinade. Compliance for plant-based analogues falls under Codex STAN 192-1995 INS 621 GMP, EU 1333/2008 E 621 quantum satis, and 21 CFR 182.1 GRAS. The twin-screw extruder typically operates at L/D 32–40, barrel temperatures 130–160 °C, and moisture 55–70%, followed by a cooling die that prevents raw fiber expansion and fixes anisotropic texture. The amount of MSG added to the dry side before the extruder is constrained by the availability of free water and the presence of reducing sugars from protein concentrates; co-injection of glucose or maltose during extrusion can reduce measurable free glutamate through Maillard reactions under shear. Post-extrusion flavoring consists of marinating wet strips in a chilled bath at 2–4 °C for 20–60 min or injecting the marinade at 10–20 wt% of the extrudate mass. Terminal products include high-moisture chunks, burger patties, sausage analogues, pulled-style pieces, and nuggets. Published data on the exact free glutamate loss in specific twin-screw configurations is limited; process validation with HPLC measurement of free glutamic acid after extrusion is recommended.

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    Certification & Compliance
    More Introduction

    Monosodium glutamate is supplied in food-grade commerce as either anhydrous sodium L-glutamate (CAS Registry Number 142-47-2) or the crystalline monohydrate (CAS Registry Number 6106-04-3); the monohydrate dominates dry seasoning blends because its crystal habit provides better flow, lower dusting, and more predictable bulk density during transfer from bulk bags into loss-in-weight feeders. The molecular formula of the monohydrate is C5H8NNaO4·H2O and its molar mass is 187.13 g/mol; the anhydrous form has a molar mass of 169.11 g/mol. Industrial production is aerobic fermentation by Corynebacterium glutamicum on starch-derived glucose or cane molasses, followed by pH adjustment with sodium hydroxide, decolorization, vacuum crystallization, centrifugation, fluidized-bed drying, and sieving into defined mesh grades. The resulting product is a white crystalline powder with a clean umami taste and a neutral pH in dilute aqueous solution. The principal model distinctions encountered in purchase specifications are anhydrous powder, crystalline monohydrate in 60–80 mesh, 80–100 mesh, and 200-mesh distributions, and low-dust agglomerated forms for high-shear dry blending.

    What Are the Contract-Specification Thresholds in the Food Chemicals Codex and How Do They Restrict Dry-Mix Use?

    Food-grade MSG is purchased against the Food Chemicals Codex monograph for monosodium glutamate. The assay acceptance range is typically 99.0–100.5% on the dried basis, with commercial certificates of analysis commonly reporting 99.5% or greater. Specific rotation [α]D20 is specified within +24.8° to +25.3° for a 10% solution in 2 N hydrochloric acid; chloride is limited to not more than 0.2%, sulfate to not more than 0.03%, lead to not more than 1 mg/kg, and arsenic to not more than 1 mg/kg in the standard monograph framework. Loss on drying for the anhydrous grade is normally set at not more than 0.5%, whereas the monohydrate is supplied with a theoretical water content of 9.62% and a practical acceptance window of 9.0–10.5%. The pH of a 5% aqueous solution is controlled to 6.7–7.2, and bulk density for 60–80 mesh crystalline monohydrate is commonly listed as 0.78–0.85 g/cm³. These values are used as incoming inspection anchors because deviations in chloride and moisture alter caking tendency, sodium equivalence, and retention of free-flowing character in dry mix packaging.

    ParameterTypical purchase specificationBasis or method
    Assay99.0–100.5% dried basisFood Chemicals Codex monograph
    Specific rotation+24.8° to +25.3°10% solution, 2 N HCl, 20°C
    Loss on drying, monohydrate9.0–10.5%Forced-air or vacuum drying
    Chloride, as NaCl≤ 0.2%Argentometric titration
    Lead≤ 1 mg/kgAtomic absorption or ICP-MS
    Bulk density0.78–0.85 g/cm³Poured bulk density, 60–80 mesh

    Applications in savory dry mixes use MSG as a crystalline umami source at addition levels from 0.1% to 0.8% of finished ready-to-eat mass, depending on the background of hydrolyzed protein, yeast extract, or tomato solids. In clear broths and bouillon granules, 0.2–0.8% MSG is commonly combined with sodium chloride and small quantities of disodium 5′-inosinate and disodium 5′-guanylate to exploit allosteric enhancement of the umami receptor. In extruded snack seasonings, 0.3–0.6% MSG on the finished product is typical, applied as a topically dusted powder after extrusion rather than as part of the melt-phase formulation when reducing sugars are present. Synergy with 5′-nucleotides is operationally relevant: a binary mixture of MSG and disodium 5′-inosinate at a weight ratio of 95:5 to 80:20 can produce a stronger umami response than the same total mass of MSG alone, allowing sodium and cost reduction. The effect is most reliable at product pH between 5.5 and 7.0; at pH below 4.5, perceived umami intensity may decrease and acid-hydrolyzed cereal notes become more noticeable in long-shelf-life dressings.

    Fermentation-Derived Trace Metal and Chloride Control Limits

    Within fermentation-based production routes, the impurity profile is managed through downstream deashing, ion exchange, and crystallization. Residual chloride arises from pH adjustment with hydrochloric acid or from process water hardness, while sulfate and iron are controlled by cation-exchange treatment and activated carbon. The FCC monograph and supplier certificates of analysis typically set chloride at not more than 0.2%, sulfate at not more than 0.03%, iron at not more than 10 mg/kg, lead at not more than 1 mg/kg, and arsenic at not more than 1 mg/kg. In dry-mix operations, chloride above 0.2% contributes to hygroscopic bridging in hoppers and false weigh-cell readings; therefore, incoming raw material is passed through a 40-mesh sweep before use. The material is stable under normal ambient storage but caking is observed in unlined paper sacks at relative humidity above 70% for periods longer than 72 h; multiwall paper bags with 0.05 mm polyethylene liners, 25 kg net weight, or bulk tote liners are standard. For high-volume snack seasoning factories, crystal size distributions of 60–80 mesh and 80–100 mesh are common because they provide adequate dispersion without excessive dusting. Fine 200-mesh monohydrate is used in clear liquid applications or where rapid dissolution is required, but it requires dust control and greater anti-caking management.

    Compared with sodium chloride, MSG contributes substantially less sodium per gram because the monohydrate contains 12.28% sodium by mass, while sodium chloride contains 39.34% sodium. In a reduced-sodium bouillon project, replacing 20% of sodium chloride by weight with MSG lowers the sodium content of the dry mix by approximately 11–13%, but the formulation must be rebalanced for water activity, chloride taste, and potassium chloride bitterness. MSG does not depress water activity as strongly as the same mass of sodium chloride; therefore, in intermediate-moisture sauces with water activity near 0.90, substitution should not exceed 15–20% unless humectants or antimicrobial hurdles are adjusted. Unlike sodium chloride, MSG has a low but measurable umami threshold and a buffering action that can shift pH of low-acid blends by 0.1–0.3 pH units in applications above 1% use. The difference is important in shelf-stable meat marinades subject to Clostridium botulinum control under reduced-salt protocols.

    When Partial Replacement Ratios Exceed 20% in Reduced-Sodium Liquid Seasoning Systems

    A sodium reduction target above 20% in clear soups and sauces cannot be achieved by MSG alone without producing an unbalanced savory profile and a slight brothy aftertaste. The practical replacement ceiling for MSG in sodium reduction is often set at 25% of the original sodium chloride mass in liquid seasonings; beyond this level, formulators combine 5–10% MSG with potassium chloride, yeast extract, and disodium inosinate/guanylate to maintain salt impression. The comparative sodium contribution and function of common crystalline ingredients are summarized in the table below. In these systems, sodium contribution is calculated on the dried ingredient mass and verified by inductively coupled plasma optical emission spectrometry after ashing; the relevant compliance limit for reduced-sodium claims is defined in country-specific nutrition labeling regulations, such as Regulation (EC) No 1924/2006 for European Union comparative claims. Process control is more demanding at replacement ratios above 20% because mineral salt blends can stratify in ribbon blenders if bulk density differences exceed 0.15 g/cm³; manufacturing lines using high-shear paddle mixers with 10–15 min blend times have lower assay variance than gravity-fed tumbling blenders.

    IngredientSodium content by massPrimary savory functionPrincipal formulation constraint
    Monosodium glutamate monohydrate12.28%Umami enhancementCaking above 70% RH; browning with reducing sugars at high temperature
    Sodium chloride39.34%Saltiness and water activity depressionSodium contribution
    Potassium chloride0% sodiumSaltiness alternativeBitter/metallic aftertaste above 30% replacement

    Compared with yeast extract and hydrolyzed vegetable protein, MSG provides a narrower, more immediate umami peak without the roasted, bouillon-like peptide background or color contribution. Yeast extract contains protein, amino acids, peptides, and nucleotides, and its glutamate content typically ranges from 2% to 12% by dry mass depending on autolysis and drying conditions; its sodium content varies from 0.2% to 5%. Hydrolyzed vegetable protein can contribute 10–30% glutamic acid content but also introduces brown color, characteristic process flavors, and, in acid-hydrolyzed products, 3-chloropropane-1,2-diol residues controlled under relevant contaminant limits. MSG is preferred when the goal is umami enhancement without changing the color, allergen labeling, or particulate identity of a dry mix. Nucleotide enhancers such as disodium 5′-inosinate and disodium 5′-guanylate have no independent umami at practical use levels but intensify the glutamate signal; they are not direct substitutes for MSG.

    In twin-screw extruded snack manufacture, MSG is generally held out of the melt phase when reducing sugars and high barrel temperatures are combined because Maillard browning can reduce visible surface brightness and generate Strecker aldehydes. Production-scale handling of corn-based extruded snacks more commonly uses external spray-oil adhesion followed by dusting with a preblended seasoning containing MSG at 0.3–0.6% of finished product mass, sodium chloride, maltodextrin, and anti-caking agents. For dry soup mixes, MSG monohydrate at 0.2–0.8% is dry-blended with salt, sugar, fat powder, and starches in a ribbon blender; the batch is discharged at 20–25°C and 40–50% relative humidity to prevent moisture pickup. Filled multiwall bags are heat-sealed and stretch-wrapped. In liquid seasoning manufacture, MSG is predissolved in water at 30–40°C before addition to steam-jacketed kettles, because direct powder addition to hot brine can create undissolved fines that accumulate in plate heat exchangers. These process choices reduce variation in fill weight, pump flow, and final sodium assay.

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