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Glucono-delta-Lactone

    • Product Name: Glucono-delta-Lactone
    • 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
    Productname Glucono-delta-Lactone
    Synonyms D-Gluconic acid delta-lactone; D-Glucono-1,5-lactone; GDL; E575
    Casnumber 90-80-2
    Ecnumber 202-016-5
    Einumber E575
    Molecularformula C6H10O6
    Molecularweight 178.14 g/mol
    Appearance White crystalline powder
    Odor Odorless
    Taste Mildly acidic
    Meltingpoint 150-153 °C
    Decomposition Decomposes at melting point
    Solubilityinwater Soluble, approx. 590 g/L at 20 °C
    Solubilityinethanol Slightly soluble
    Ph 2.5-3.5 (aqueous solution, concentration dependent)
    Assay 99.0-100.5%
    Moisture ≤0.5%
    Ash ≤0.1%
    Heavymetals ≤10 mg/kg
    Arsenic ≤3 mg/kg
    Lead ≤2 mg/kg
    Specificrotation +63.5° (c=1, water)
    Density 1.6 g/cm³ approx.
    Bulkdensity 0.6-0.8 g/cm³ approx.
    Stability Stable under normal conditions; hydrolyzes in water
    Hygroscopicity Non-hygroscopic
    Pka 3.86 (gluconic acid, 25 °C)
    Use Acidifier; leavening agent; sequestrant; protein coagulant
    Storage Cool, dry, well-ventilated area
    Shelflife 2 years typical

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

    Packing & Storage
    Packing Glucono-delta-Lactone is packaged in 25 kg net weight, moisture-resistant, polyethylene-lined fiber drums with sealed inner liners for industrial use.
    Container Loading (20′ FCL) The chemical Glucono-delta-Lactone is bagged in 25 kg units, palletized, and securely stuffed into a 20-foot FCL container for export.
    Shipping Glucono-delta-Lactone is typically shipped as a non-hazardous, food-grade white crystalline powder in sealed polyethylene-lined bags, fiber drums, or cartons. Store and transport in a cool, dry, well-ventilated area away from moisture, strong oxidizers, and odors. No special dangerous goods labeling required.
    Storage Store glucono-delta-lactone in a cool, dry, well-ventilated area, protected from moisture and humidity. Keep containers tightly closed, clearly labeled, and away from heat, flames, and strong oxidizing agents. Maintain good housekeeping to prevent dust accumulation. Use secondary containment where required, and follow manufacturer instructions, local regulations, and workplace safety procedures.
    Shelf Life Dry Glucono-delta-lactone has a shelf life of about two years when stored cool, dry, and sealed; solutions should be prepared fresh.
    Application of Glucono-delta-Lactone
    In soy protein gelation, glucono-delta-lactone is dispersed into chilled soy milk at 4–10°C before thermal processing begins. The cyclic ester undergoes ring-opening hydrolysis to gluconic acid at a rate that remains low in the chilled suspension but accelerates sharply once the continuous stream reaches 80–85°C. Addition of 0.25–0.35% by weight of soy milk produces a coagulum pH of 5.4–5.6 without the bitter chloride aftertaste linked to magnesium-based coagulants. On production lines using plate heat exchangers and sealed polypropylene forming tubs, the GDL-soy milk mixture is held at 85–90°C for 25–40 min; the curd is then cut and cooled in the package. Because the acid is generated in situ rather than dosed as free acid, the soy protein aggregates uniformly from the liquid phase, which reduces surface syneresis and cracking in the final block. Food-grade compliance is anchored in FDA 21 CFR 184.1318 and Commission Regulation (EU) No 231/2012; the material is listed as INS 575 under Codex STAN 192-1995. The terminal product is silken or soft tofu. Operations targeting firm tofu normally blend GDL with calcium sulfate at 0.10–0.20% because GDL alone does not provide the calcium cross-linking required for high-pressure mechanical pressing.

    What Controls Carbon Dioxide Release in Refrigerated Dough Leavening?

    In chemically aerated dough, GDL functions as a slow-release acidulant for sodium bicarbonate. Unlike fast-acting monocalcium phosphate monohydrate, GDL hydrolyzes only after free water migrates into the starch-protein matrix and the dough temperature rises above 15–20°C. The reaction consumes one mole of sodium bicarbonate per mole of gluconic acid and releases carbon dioxide, sodium gluconate, and water. Formulators calculate the acid requirement from the neutralization value of GDL; when 100 g of GDL neutralizes approximately 45–50 g of sodium bicarbonate, a batter containing 1.5% sodium bicarbonate on flour weight requires 3.0–3.3% GDL to avoid residual alkalinity in the crumb. In industrial muffin and pound cake lines, GDL is dry-blended with flour, starch, and sodium bicarbonate; the batter is mixed below 18°C and baked in continuous band ovens at 170–200°C. Delayed gas release supports controlled crumb expansion during the first 8–12 min of baking, when starch gelatinization is occurring and gas cell walls are most deformable. The finished crumb pH typically lands between 6.8 and 7.2, which limits soapy sodium carbonate notes. Terminal products include refrigerated biscuit dough, frozen muffin batter, pound cakes, and scones. Compliance references include the Food Chemicals Codex monograph for glucono-delta-lactone, FDA 21 CFR 184.1318, and Regulation (EU) No 231/2012. Overdosing above the stoichiometric requirement leaves residual sodium gluconate, which increases crumb hygroscopicity and can reduce shelf-crispness in frozen products.

    Processed meat emulsions are acidified with GDL to suppress psychrotrophic spoilage flora during cold storage, but the addition rate must be controlled to avoid emulsion collapse. In finely comminuted cooked sausage batters, GDL is added at 0.5–1.0% of the meat block weight. The gradual hydrolysis shifts batter pH from approximately 6.2 toward 5.3–5.5 as the product moves through chilled holding and smokehouse heating. Because the pH drop moves meat proteins toward their isoelectric point, water-holding capacity declines; to compensate, 0.3% sodium tripolyphosphate is typically incorporated before GDL addition. Vacuum bowl cutters operating at 3,000 rpm generate frictional heat that accelerates GDL hydrolysis, so batter temperature must be kept below 12°C to prevent premature acid gelation of the myofibrillar matrix. The emulsion is stuffed into cellulose or collagen casings and heat-processed to a core temperature of 72–75°C. Terminal products include skinless frankfurters, bologna, and shelf-stable meat snacks. Regulatory verification is required against USDA FSIS Directive 7120.1 and Regulation (EC) No 1333/2008 for the specific meat category. GDL is not a direct replacement for traditional lactic acid fermentation in dry-cured sausages; in those systems, rapid acidification with GDL above the stated range can produce brittle texture, excessive purge, and off-flavor from residual gluconate.

    When Glucono-delta-Lactone Replaces Cultured Acidification in Acid-Coagulated Cheese

    In acid-coagulated cheese manufacture, GDL provides reproducible pH reduction without the 16–24 h fermentation window and bacteriophage sensitivity associated with mesophilic starter cultures. For direct acidification of pasteurized whole milk at 35–38°C, GDL is dosed at 0.3–0.6% by weight of milk; the target curd pH for paneer and queso blanco is 5.2–5.4, reached within 20–40 min under gentle agitation. The coagulated curd is then drained and pressed at 0.5–1.0 kg/cm². Because GDL does not generate lactic acid, the resulting cheese has a clean acid profile that supports flavored curd bases but limits the formation of diacetyl and other fermentation-derived aroma compounds. Dosing is preferably performed by predispersing GDL in a slip stream of cold milk before introducing it into the main vat; this avoids localized pH pockets that create grainy curd defects. Compliance is covered under FDA 21 CFR 184.1318 and Regulation (EC) No 1333/2008 for dairy products where acidity regulators are permitted. Terminal products include paneer, queso blanco, and acid-curd dessert preparations. GDL is not suitable for rennet-coagulated hard cheese manufacture because the rapid acidification alters calcium phosphate equilibrium and curd mineral content before adequate rennet action can occur.

    Personal care formulations employ gluconolactone as a slow-release polyhydroxy acid and metal sequestrant. In aqueous leave-on exfoliants at pH 3.5–4.0, inclusion rates of 1–5% w/w provide gradual gluconic acid release over 24–72 h at ambient temperature; the lower instantaneous free-acid concentration reduces the stinging response associated with glycolic acid at equivalent pH. The ring-opened gluconate moiety chelates ferric and cupric ions, which supports oxidative stability in ascorbic acid serums and reduces discoloration caused by polyphenol-metal complexes. Processing requires dispersion in the water phase at or below 40°C; because hydrolysis continues after compounding, the finished batch must be back-titrated with sodium hydroxide to meet final pH specification. Stability documentation commonly follows ISO 17516:2014 for microbiological limits and ISO 11930 for preservative challenge testing. Gluconolactone is listed by INCI name and is not prohibited under Regulation (EC) No 1223/2009; the Cosmetic Ingredient Review Expert Panel has reviewed its safety in leave-on and rinse-off formulations. Terminal products include exfoliating toners, anti-aging serums, and rinse-off gel cleansers.

    Chelation Performance in Alkaline Cleaner Formulations

    GDL is used as a biodegradable complexing agent in bottle-washing and clean-in-place applications where aminopolycarboxylate chelants such as EDTA and NTA face discharge restrictions. In caustic bottle-washing baths containing 2–5% sodium hydroxide at 70–80°C, GDL is dosed at 1–2% of bath volume and hydrolyzes rapidly to gluconate. The open-chain gluconate forms soluble complexes with calcium, magnesium, and ferric ions, preventing scale deposition on spray nozzles, bottle surfaces, and heat exchanger plates. Chelation efficiency depends on free alkalinity and temperature; formulators should validate performance through pilot-scale hardness challenge testing rather than relying on vendor nominal chelation values. GDL is predissolved in warm water before metering into the alkaline bath to avoid localized acid neutralization and exothermic spatter. Because gluconate is readily biodegradable under OECD 301B conditions, the resulting effluent has lower residual chelant persistence than EDTA-based formulations. Published data for high-alkali heavy-metal chelation under specific load conditions is limited, and GDL is generally less effective than phosphonates for ferric ion control in strongly alkaline systems. Terminal products include CIP alkaline cleaners, bottle-washing formulations, and descalers for dairy and beverage process lines.

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    Certification & Compliance
    More Introduction

    Glucono-delta-lactone (GDL; CAS 90-80-2, additive E575) is the intramolecular 1,5-lactone of D-gluconic acid, supplied as a white to off-white crystalline powder with a molecular weight of 178.14 g mol⁻¹, a melting range of approximately 151–155 °C with decomposition, and an aqueous solubility near 59 g/100 mL at 25 °C. Food-grade material placed on the EU market under Regulation (EC) No 1333/2008 and declared against the Food Chemicals Codex monograph is controlled for assay at ≥99.0 % on the dried basis as C₆H₁₀O₆, moisture ≤0.5 %, lead ≤2 mg/kg, arsenic ≤1 mg/kg, sulfate ≤0.03 %, and reducing substances ≤0.5 %. Supplier-specific product designations include fine powder, granular, and 200-mesh grades; selection is usually made on the basis of dust containment, dissolution rate, metering accuracy, and feeder behavior rather than assay differences. Aqueous dissolution is followed by ring-opening hydrolysis to gluconic acid, so a 1 % dispersion does not show an immediate equilibrium pH but evolves to approximately 2.5–3.5. This hydrolysis lag is the principal technical distinction from directly ionizing organic acids such as citric, lactic, or acetic acid.

    What Determines Acid Release Kinetics in High-Moisture Formulations?

    The conversion of GDL to gluconic acid follows pseudo-first-order ring-opening hydrolysis that accelerates with increasing temperature and with available water activity. At 4 °C the hydrolysis is deliberately retarded, permitting prepared slurries or batters to be held before gelation; at 70–85 °C acid release approaches completion within minutes. In continuous tofu or dairy processing, the pH recorded at the filler is therefore a function of residence time, back-pressure, and heat-exchanger outlet temperature rather than solely the mass of GDL added. Conductivity sensors often respond more reliably than glass pH electrodes in high-protein suspensions because electrode fouling creates a measurement lag. The kinetics also impose a processing boundary: adding GDL to an already hot and viscous batter can localize acid release before the mixer disperses the powder, producing low-pH zones visible as graininess or serum pockets in the final gel. In low-water systems such as dry bakery mixes with water activity below 0.6, hydrolysis remains inhibited during storage, but rehydration initiates acid release within the batter. Phosphate buffers in meat emulsions consume the first fraction of released acid; the effective GDL dose may need to be increased by 0.1–0.2 percentage points in buffered systems to reach the same final pH.

    In oilfield cement slurries and cementitious grouting, GDL has been evaluated as a delayed acid source for controlled pH reduction and as a component of set-retarding packages. Slurry behavior should be confirmed with a rotational viscometer operated according to API RP 10B-2, particularly at bottomhole circulating temperatures above 60 °C, where accelerated hydrolysis can shorten the retarder effect. Published field data for this specific configuration is limited; thickening-time curves should be regenerated with the actual job water and cement because dissolved salts and lignosulfonate-based retarders alter buffer capacity and acid-release profile.

    Soy Protein Coagulation and Curd Texture Control

    In tofu manufacturing, GDL is metered into soy milk at 0.25 % to 0.35 % by mass before tray filling. Coagulation proceeds through a gradual pH decline from approximately 6.7 to 5.5–5.8, reducing electrostatic repulsion near the isoelectric points of the 7S β-conglycinin and 11S glycinin fractions. Unlike calcium sulfate or magnesium chloride, GDL contributes no cation-linked protein bridging; gel formation is therefore pH-driven and yields a smooth, silken texture with minimal added mineral content. Production-scale texture variation is commonly traced to the 11S/7S ratio and total solids concentration. At equivalent pH, high 11S/7S milk generally produces a firmer gel, which may require reducing the GDL dose by 0.05–0.1 percentage points to maintain target firmness. Small-amplitude oscillatory shear measurements show that storage modulus G′ rises sharply only after the pH enters the critical gelation region; this lag can be exploited for cup filling but demands strict hold-time control. Dual coagulant systems combining GDL with 0.1–0.3 % calcium sulfate are used when firmer pressed curd is required, but calcium sulfate above 0.4 % can cause chalky mouthfeel and whey separation.

    In dry bakery mixes, GDL functions as a delayed leavening acid. The stoichiometric neutralization ratio is 2.12 g GDL per 1 g sodium bicarbonate, derived from molecular weights 178.14 g mol⁻¹ and 84.01 g mol⁻¹; commercial formulas usually operate below this ratio to leave residual bicarbonate and prevent premature gas loss during depositing. Because hydrolysis shows a lag phase, carbon dioxide evolution occurs predominantly during baking rather than during mixing, which is useful in high-speed cake and wafer batter lines. In comminuted meat systems, GDL may be added at 0.5–1.0 % of batter weight to lower pH to 5.2–5.6 over several hours at 20–25 °C, accelerating color development and reducing water activity. This acidification does not reproduce the volatile profile of starter-culture fermentation; diacetyl, acetoin, and proteolytic peptide generation are absent, so the sensory result is cleaner but less complex.

    When GDL Replaces Citric or Lactic Acid in Cold-Process Formulations

    In cold-fill beverages, dressings, or dairy desserts where immediate pH adjustment is required, direct substitution of citric or lactic acid with GDL will not replicate the initial pH drop. The lag phase can be advantageous for viscosity development, package sealing, or delayed gelation, but it may be a liability in short residence-time cold processes. The table below compares typical behavior in aqueous systems; values should be treated as formulation starting points rather than universal specifications.

    ParameterGDLCitric acid monohydrateLactic acid 80 %Acetic acid
    Molecular weight178.14 g mol⁻¹210.14 g mol⁻¹90.08 g mol⁻¹60.05 g mol⁻¹
    First dissociation constant of corresponding acidpKₐ 3.86 for gluconic acidpKₐ₁ 3.13pKₐ 3.86pKₐ 4.76
    Typical pH of 1 % aqueous solution2.5–3.5 after hydrolysis2.0–2.22.3–2.52.5–2.8
    Acidification profileLag, then progressiveImmediateImmediateImmediate
    Sensory impactMild sweet aftertaste followed by acidSharp, rapid sournessSour with slight dairy notePungent vinegar note
    Tofu coagulation suitabilityPrimary coagulantNot used aloneNot used aloneNot used alone

    In dry beverage bases and protein powder blends, the neutral taste of the intact lactone permits acidulation to emerge only after reconstitution. This differs from citric acid, which imparts immediate sourness even in dry form when it contacts saliva or residual moisture. GDL also exhibits chelation of calcium and heavy metal ions after hydrolysis to gluconate, but its sequestering capacity in acid solution is lower than that of citric acid. In alkaline cleaning formulations, GDL can be combined with sodium hydroxide to generate sodium gluconate in situ, avoiding the handling and freezing-point constraints of liquid gluconic acid. That reaction is exothermic; alkali concentrations above 10 % should not be combined with dry GDL without cooling because localized heat release can cause boiling at the powder-liquid interface.

    Regulatory Monograph Limits and Certificate-of-Analysis Checklist

    Compliance documentation should align with the Food Chemicals Codex monograph, the EU food additive specification for E575, and the United States GRAS affirmation. The table summarizes a representative acceptance checklist for a food-grade lot.

    ParameterAcceptance criterionReference or method
    AppearanceWhite to off-white crystalline powderVisual inspection
    Assay, C₆H₁₀O₆, dried basis≥99.0 %FCC 14 monograph
    Moisture≤0.5 %Karl Fischer titration
    Lead≤2 mg/kgFCC 14 / ICP-MS
    Arsenic≤1 mg/kgFCC 14
    Sulfate≤0.03 %FCC 14
    Reducing substances≤0.5 %FCC 14
    FDA statusGRAS, GMP use21 CFR 184.1318
    EU statusPermitted quantum satis in most categoriesRegulation (EC) No 1333/2008 Annex II
    JECFA evaluationADI not specifiedJECFA monograph

    Dry GDL powder is stable in sealed packaging, but exposure to relative humidity above 60 % initiates hydrolysis, causing caking, assay loss, and eventual formation of free gluconic acid. Storage should be maintained in closed containers at 10–30 °C under dry conditions. When preparing slurries, GDL should be added to water under agitation rather than water added to powder; concentrated slurries will continue to acidify and should be used before the equilibrium pH is reached when delayed acidification is intended. In dry blends with sodium bicarbonate, moisture ingress must be prevented because the acid-base reaction can initiate prematurely. GDL should not be dry-blended with strongly basic or amine-containing additives in concentrated form; premature neutralization releases heat and reduces the acid-release capacity needed for later processing stages. Food-grade GDL is not classified as hazardous under normal EU CLP criteria, but dust generation during milling, sieving, or transfer should be controlled with local exhaust ventilation to avoid respiratory irritation.

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