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Pharmaceutical Grade Lactic Acid

    • Product Name: Pharmaceutical Grade Lactic Acid
    • Factroy Site: Wusu, Tacheng Prefecture, Xinjiang, China
    • Price Inquiry: sales7@alchemist-chem.com
    • Manufacturer: Alchemist Worldwide Ltd
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    Specifications
    HS Code 515899
    Product Pharmaceutical Grade Lactic Acid
    Chemical Name 2-Hydroxypropanoic acid
    Chemical Formula C3H6O3
    Molecular Weight 90.08 g/mol
    Cas Number 50-21-5
    Einecs Number 200-153-7
    Appearance Colorless to pale yellow syrupy liquid
    Odor Slight characteristic odor
    Assay 88.0%-92.0% (w/w) of C3H6O3, on anhydrous basis
    Water Content 8.0%-12.0% (w/w)
    Specific Gravity 1.20-1.21 at 20°C
    Boiling Point 122°C at 15 mmHg
    Melting Point 16.8°C (racemic form)
    Pka 3.86 at 25°C
    Solubility Miscible with water and alcohol; sparingly soluble in ether
    Ph 1.5-2.5 for a 0.1 M aqueous solution
    Storage Conditions Keep in tightly closed container, protected from light, at controlled room temperature

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

    Packing & Storage
    Packing Packaged in 25 kg HDPE drums with tamper-evident seals, labeled for pharmaceutical-grade purity and safe handling.
    Container Loading (20′ FCL) Pharmaceutical Grade Lactic Acid shipped in a 20′ FCL, packed in drums/IBCs, securely palletized and ventilated.
    Shipping Pharmaceutical Grade Lactic Acid ships as UN3265, Corrosive Liquid, Acidic, Organic, N.O.S., Class 8, Packing Group III. It is transported in HDPE drums or IBCs with proper labels, segregation from alkalies and oxidizers, and temperature-controlled, spill-containment measures. Ensure secure upright loading and adequate ventilation.
    Storage Store Pharmaceutical Grade Lactic Acid in a tightly sealed, corrosion-resistant container, away from moisture and direct sunlight. Keep in a cool, dry, well-ventilated area, at controlled room temperature, separated from strong oxidizers, bases, and metals. Maintain container integrity to prevent contamination, and ensure clear labeling for traceability and safety.
    Shelf Life Shelf life is 2 years from manufacture when stored unopened at controlled room temperature, protected from light and moisture.
    Application of Pharmaceutical Grade Lactic Acid

    Does Glucose Degradation in Lactate-Buffered Peritoneal Dialysis Fluid Constrain Autoclave Cycle Design?

    In commercial peritoneal dialysis fluid manufacturing, pharmaceutical-grade lactic acid is not retained as free acid in the finished solution but serves as the titratable acid source for generating the lactate buffer system. A formulation containing 1.5% anhydrous dextrose monohydrate, 5.67 g/L sodium chloride, 3.92 g/L sodium lactate, 0.257 g/L calcium chloride dihydrate, and 0.152 g/L magnesium chloride hexahydrate is titrated with 3.15–3.60 g/L pharmaceutical-grade lactic acid on an anhydrous basis to a pre-autoclave pH of 5.4–5.5 at 20–25 °C. The finished solution specification is pH 5.0–5.5, verified by USP <791> and Ph. Eur. 2.2.3. The lactic acid source must meet the USP-NF Lactic Acid monograph assay range of 88.0–92.0% w/w, with bacterial endotoxin and sterility assurance aligned to USP <85> and USP <71> for the finished heat-sterilized product. Production is carried out in a 316L stainless-steel vessel with an electropolished surface finish of Ra ≤0.8 μm; lactic acid is introduced under low-turbulence impeller agitation at 30–60 rpm, followed by sodium hydroxide solution to produce the lactate buffer, and then electrolytes and dextrose are dissolved. The filled polyvinyl chloride-free bag is steam-sterilized at 121 °C for ≥15 min with a minimum F0 of 8. The main process conflict is glucose caramelization and 5-hydroxymethylfurfural formation under thermal load; therefore pH adjustment, dissolved oxygen control, and fill-volume headspace are monitored as in-process parameters. Terminal product types include 1.5%, 2.5%, and 4.25% dextrose lactate-buffered peritoneal dialysis solutions packaged in flexible containers.

    Keratolytic Cream pH Drift and Esterification Controls During Vacuum Emulsification

    Topical semi-solid formulations for hyperkeratotic dermatological conditions incorporate pharmaceutical-grade lactic acid at two distinct addition levels: 0.5–2.0% w/w as a humectant and pH-modifying excipient, and 10–12% w/w as a keratolytic active component. The finished emulsion is adjusted to pH 3.5–4.5, with potentiometric verification on the undiluted product under USP <791> or Ph. Eur. 2.2.3. In a typical oil-in-water cream manufacturing sequence, the aqueous phase containing lactic acid, glycerin, and purified water is held at 40–45 °C, while the oil phase containing cetostearyl alcohol, white petrolatum, and nonionic emulsifier is melted at 70–75 °C. The phases are combined in a vacuum emulsifying vessel equipped with an anchor stirrer operating at 10–25 rpm and a homo-mixer operating at 1,500–3,000 rpm. Lactic acid is added to the aqueous phase before homogenization rather than after phase combination to prevent localized low-pH regions from destabilizing the emulsifier film. An operational boundary is that prolonged processing above 60 °C in the presence of fatty alcohols can drive partial esterification of lactic acid, altering free acid content and shifting the keratolytic release profile. Terminal product forms include medicated creams, lotions, and anhydrous ointment bases in laminated aluminum or high-density polyethylene tubes, where the acid is pre-dissolved in propylene glycol before incorporation. Compliance for nonsterile topical products is anchored to the USP-NF Lactic Acid monograph, USP <795> for extemporaneously compounded preparations, and ICH Q3D elemental impurity limits for heavy metal control.

    In oral liquid pharmaceutical manufacturing, pharmaceutical-grade lactic acid functions as a low-taste acidulant and pH stabilizer for drug substances requiring an acidic microenvironment for chemical stability. The addition ratio is 0.1–2.0% w/v, titrated to a target pH of 3.0–4.0; the specific amount is derived from a pH titration curve established for each buffer system because lactic acid has a pKa of 3.86 at 25 °C and provides buffering capacity approximately ±1 pH unit around this point. Manufacturing is performed in jacketed 316L stainless-steel vessels with a propeller impeller operating at 50–150 rpm; the active pharmaceutical ingredient is dissolved in purified water, lactic acid is added as a 10% w/v diluted solution, and pH is monitored continuously until the formulation reaches 3.5–4.0 before addition of preservatives, sweeteners, and viscosity modifiers. Terminal product types include oral syrups, suspension reconstitution bases, and pediatric oral solutions filled into amber glass or high-density polyethylene bottles. The compendial standard for the acid source is the USP-NF Lactic Acid monograph, with pH verification under USP <791>; preserved oral solutions also undergo antimicrobial effectiveness testing under USP <51>. A processing limitation is that lactic acid should not be added to a hot syrup base above 50 °C because acid-catalyzed sucrose inversion increases during cooling stages; published data for this specific configuration is limited, but inversion can be tracked by polarimetry as an in-process control.

    If Residual Lactide Hydrolysis Accelerates PLGA Microsphere Degradation, Polymer Drying Must Precede Extrusion

    Pharmaceutical-grade lactic acid is the precursor for lactide and, through ring-opening polymerization, for poly(lactide-co-glycolide) used in controlled-release parenteral implants and microspheres. In this application, lactic acid is not directly added to the drug formulation; it is first oligomerized, cracked to L-lactide or D,L-lactide, and then copolymerized at defined lactide-to-glycolide feed molar ratios. The feed ratio determines the degradation half-life and release profile of the finished polymer. The table below lists representative PLGA grades used in microsphere and implant manufacturing lines.

    PLGA copolymer grade and processing specification
    Lactide/glycolide feed molar ratioIntrinsic viscosity range in chloroform at 25 °C (dL/g)Residual lactide monomer limitTypical terminal form
    50:500.15–0.25≤0.5% w/wMicrospheres
    75:250.25–0.40≤0.5% w/wMicrospheres / in situ implant
    85:150.50–1.20≤0.5% w/wExtruded implant / suture

    After polymerization, the copolymer is precipitated, washed, and vacuum-dried to a residual lactide monomer content below 0.5% w/w and residual moisture below 0.02% w/w before extrusion or solvent-based processing; residual lactide hydrolysis generates lactic acid inside the polymer matrix and lowers local pH, which accelerates autocatalytic degradation. For microsphere manufacture, PLGA is dissolved in dichloromethane at 10–20% w/v and emulsified into an aqueous continuous phase containing 0.5–2.0% polyvinyl alcohol under overhead stirring at 300–800 rpm; solvent removal is conducted at 25–35 °C under reduced pressure, and the hardened microspheres are washed and lyophilized. For extruded implants, a twin-screw extruder with an L/D ratio of 25:1 and controlled zone temperatures of 130–180 °C is used under nitrogen purge to limit thermo-oxidative degradation. Compliance testing includes ISO 10993-5 cytotoxicity, ISO 10993-10 irritation and sensitization, ISO 10993-11 systemic toxicity, and ASTM F1635-16 for in vitro degradation of hydrolytically degradable surgical implants. Terminal product types include PLGA microspheres for subcutaneous or intramuscular injection, in situ forming implants, and braided surgical sutures.

    In concentrated topical keratolytic collodion preparations, pharmaceutical-grade lactic acid is combined with salicylic acid in a flexible collodion base to treat common warts, corns, and calluses. The addition ratio is 10–20% w/w lactic acid and 10–20% w/w salicylic acid; finished product pH is not a meaningful control because the nonaqueous collodion vehicle has limited water activity, so free acid content and uniformity of the dried film are verified instead. Manufacturing is carried out in closed stainless-steel or glass-lined vessels under explosion-proof electrical classification because the vehicle contains ethanol and diethyl ether; salicylic acid is dissolved first in the ethanol-ether portion, lactic acid is then metered into the solution at 15–25 °C, and flexible collodion is added with low-shear mixing at 20–50 rpm. The solution is filled into amber glass bottles with PTFE-lined closures to limit solvent loss and moisture ingress. Compliance for the finished compounded preparation is governed by USP <795> when prepared in a pharmacy, while the acid components must meet the USP-NF Lactic Acid and USP-NF Salicylic Acid monographs. Finished batch release includes loss on drying, residue on evaporation, and viscosity by Brookfield rotational viscometer at 25 °C, spindle LV-2, speed 12 rpm. Terminal product types include topical wart collodion paints and callus softening lacquers packaged as brush-on or dropper-applied units. An operational boundary is that lactic acid and salicylic acid mixtures can precipitate if the ethanol-to-ether ratio falls below the solvent balance specified in the batch record; published data for this specific configuration is limited, so the ratio is controlled by in-process refractive index measurement.

    Vaginal Bioadhesive Gels Require a Narrowed pH 3.5–4.2 Window for Mucoadhesion

    Lactic acid is used in vaginal pH-modulating gels at addition ratios of 0.5–2.0% w/w to restore or maintain the vaginal pH range of 3.5–4.2 after microbial imbalance. The formulation platform typically comprises a crosslinked acrylic acid polymer such as carbomer or polycarbophil at 0.5–1.5% w/w, purified water, humectant, and preservative. The manufacturing process begins with cold hydration of the polymer in purified water under high-shear dispersion at 600–1,200 rpm in a vacuum planetary mixer; pharmaceutical-grade lactic acid is added as a 10% w/v solution, and the gel is then partially neutralized with 18% w/w sodium hydroxide to build viscosity and bioadhesive yield stress. The endpoint pH is verified with a surface electrode conforming to USP <791> or Ph. Eur. 2.2.3 after homogenization; over-neutralization above pH 4.2 reduces hydrogen-bonding-mediated mucoadhesion and must be avoided. Finished gels are filled into aluminum or high-density polyethylene tubes with narrow-diameter orifice tips. Compliance is anchored to the USP-NF Lactic Acid monograph, USP <51> antimicrobial effectiveness testing for preserved formulations, and the Ph. Eur. monograph for semi-solid preparations for vaginal use. Terminal product types include single-use vaginal gel tubes, applicator pre-filled systems, and combination products incorporating pH sensor film. The processing boundary is that entrained air during high-shear mixing increases yield stress unpredictably; vessels are therefore operated under vacuum at −0.7 to −0.9 bar during the final homogenization step.

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    Certification & Compliance
    More Introduction

    Pharmaceutical Grade Lactic Acid is supplied as a purified aqueous solution of 2-hydroxypropanoic acid with the CAS 79-33-4 designation for the L(+) enantiomer and CAS 50-21-5 for the racemic mixture. Compounding pharmacies and finished-dose manufacturers typically order the product by concentration-grade models such as L(+)-Lactic Acid 90% USP-NF/Ph. Eur. or L(+)-Lactic Acid 88% JP. The nominal total acid content is controlled between 88.0% and 92.0% w/w, expressed as C₃H₆O₃, but the solution is not a simple monomer; it exists as an equilibrium mixture of free lactic acid, linear condensation dimers, trimers, and water. Pharmaceutical grade status is defined less by total acidity and more by the absence of bacterial endotoxins, heavy metals, residual solvents, and the D-lactic acid fraction. A representative release profile specifies L-isomer ≥ 97.5% and D-isomer ≤ 2.5%, whereas technical or food acidulants frequently leave the enantiomeric ratio uncontrolled or wider. This distinction matters in parenteral and dialysis applications because D-lactate is metabolised more slowly in humans than L-lactate.

    Manufacturing of pharmaceutical grade lactic acid normally proceeds by anaerobic homofermentative conversion of glucose or sucrose using selected Lactobacillus strains, followed by calcium lactate precipitation at pH 10–11 with calcium hydroxide. The calcium lactate cake is washed, acidified with sulfuric acid, and filtered to remove calcium sulfate. The clarified acid is then processed through activated carbon, cation-exchange resin, and anion-exchange resin to reduce colour, iron, sulfate, and residual sugars, and concentrated in wiped-film evaporators at 60–80 °C under reduced pressure. The final solution is passed through a 0.2 µm sterilising-grade filter into depyrogenated fluorinated high-density polyethylene packaging. Packaging models include 30 kg drums, 250 kg drums, and 1,250 kg intermediate bulk containers with nitrogen blanketing at 0.1–0.3 bar. The ion-exchange and carbon-treatment sequence is operationally critical: inadequate resin regeneration or aged carbon beds raise total organic carbon, endotoxin, and colour, and can release leached monomers that later fail Ph. Eur. 2.4.24 residual solvent or USP <467> testing.

    What Specifications Define Pharmaceutical Grade Lactic Acid?

    A representative release certificate for L(+)-lactic acid 90% pharmaceutical grade includes total acidity, enantiomeric purity, colour, chloride, sulfate, iron, arsenic, residual solvents, and microbial attributes. Total acidity is determined by acid-base titration with 1.0 mol/L sodium hydroxide using a potentiometric endpoint, with an acceptance window of 88.0–92.0% w/w; enantiomeric purity is confirmed by chiral ligand-exchange HPLC or by enzymatic D-lactate dehydrogenase assay. Colour is controlled at ≤ 50 APHA against platinum-cobalt reference solutions; chloride and sulfate are limited because chloride accelerates corrosion in 316L stainless steel transfer lines and sulfate can precipitate in calcium-containing dialysate concentrates. The typical chloride limit is ≤ 0.002% and sulfate ≤ 0.005%. Iron is held at ≤ 5 ppm to avoid discolouration in formulations containing phenolic antioxidants, while arsenic is limited to ≤ 1 ppm and class 1 heavy metals are governed by ICH Q3D Option 1. Endotoxin and microbial limits differentiate pharmaceutical lactic acid from food grade even when the acid content is identical.

    Representative specification profile for L(+)-lactic acid 90% pharmaceutical grade
    ParameterRelease limitMethod designation
    Assay, total acidity as C₃H₆O₃88.0–92.0% w/wPh. Eur. 2.5.3 acid-base titration
    L-isomer≥ 97.5%Chiral HPLC / enzymatic assay
    D-isomer≤ 2.5%Chiral HPLC / enzymatic assay
    Colour≤ 50 APHAPh. Eur. 2.2.2, Method II
    Chloride≤ 0.002%Ph. Eur. 2.4.4
    Sulfate≤ 0.005%Ph. Eur. 2.4.13
    Iron≤ 5 ppmPh. Eur. 2.4.20
    Arsenic≤ 1 ppmPh. Eur. 2.4.2, Method A
    Methanol≤ 50 ppmPh. Eur. 2.4.24 / USP <467>
    Bacterial endotoxins≤ 0.25 EU/mgPh. Eur. 2.6.14 / USP <85>
    TAMC≤ 100 CFU/gPh. Eur. 2.6.12 / USP <61>
    TYMC≤ 10 CFU/gPh. Eur. 2.6.13 / USP <61>

    The specification values in the above table are representative release targets for a parenteral-excipient model and should be verified against the current Ph. Eur. monograph 01/2018:0656, USP-NF Lactic Acid monograph, and JP Lactic Acid monograph. Manufacturers may tighten individual limits for specific injectable or dialysis products; for example, endotoxin may be controlled at ≤ 0.1 EU/mg when the downstream formulation already contains an endotoxin-sensitive peptide. Each batch is accompanied by a certificate of analysis that records water content, optical rotation, and non-volatile residue; compendial identity is confirmed by retention-time agreement in liquid chromatography and by the colorimetric reaction of lactate with iron(III) chloride. The product should not be released to pharmaceutical manufacture without documented absence of citric, oxalic, tartaric, and phosphoric acids, which are separately limited in the monograph to ensure the lactic acid has not been blended with cheaper acidulants.

    Chiral HPLC for the release of L-lactic acid typically uses a ligand-exchange column maintained at 30 °C with 5 mM copper(II) sulfate mobile phase and ultraviolet detection at 254 nm; the resolution between D- and L-lactate is typically ≥ 1.5. For confirmatory identity, compendial optical rotation is measured on the neat solution by Ph. Eur. 2.2.7, and total organic carbon after dilution to 10% w/v is used as an in-process check of purification quality. Conductivity after 10% w/v dilution is monitored in release to detect excessive ionic contamination from incomplete ion-exchange rinsing. The solution is also inspected for visible particulate matter after dilution because pharmaceutical grade lactic acid is intended for downstream sterile filtration; any visible fibres or resin fragments require re-filtration and a deviation investigation.

    Physically, the 90% w/w solution is a colourless to pale-yellow syrupy liquid with density 1.20–1.22 g/cm³ at 25 °C, refractive index 1.426–1.432, and dynamic viscosity 40–80 mPa·s at 25 °C. The freezing point remains below -10 °C for the 88–92% concentration range, which permits unheated tank transfer in cold storage areas. Hygroscopicity is a critical processing variable: a 90% solution stored in an open vessel at 25 °C and 75% RH absorbs atmospheric moisture and shifts the free-acid/oligomer equilibrium; repeated partial withdrawal from drums without nitrogen overlay can increase water content by 0.5–1.0% w/w over 30 days in humid production areas. Transfer lines are therefore constructed from 316L stainless steel or PTFE-lined pipework with EPDM or fluoropolymer gaskets, and centrifugal pump seals are specified for acid service at pH < 2.

    When Lactic Acid Functions as a Parenteral Excipient and Dialysis Buffer Precursor

    In injectable manufacture, pharmaceutical grade lactic acid is diluted to 0.1–2.0% w/v and added to the aqueous phase before the active pharmaceutical ingredient to depress pH into a stability window of 3.0–4.5. The weak acid has a pKa of 3.86 at 25 °C; therefore it provides useful buffer capacity in this acidic range but negligible capacity at physiological pH 7.4. Dosing is performed by slow addition to water under continuous agitation, never water to concentrated acid, because the dilution exotherm can locally exceed 8 °C in a 10% w/v preparation. Production vessels larger than 500 L typically use jacket cooling with 5–15 °C coolant and recirculation loops at 1–2 m/s to avoid pH overshoot. In-line pH probes with automatic temperature compensation are positioned downstream of the dosing point, and the addition is stopped when the product-specific pH endpoint is reached.

    For peptide or protein formulations where chloride ions are undesirable, lactic acid is selected over hydrochloric acid at concentrations below 0.5% w/v. The final formulation is often re-adjusted to pH 4.0–5.5 with dilute sodium hydroxide, and compatibility studies are required because lactic acid can chelate divalent cations and may affect the solubility of calcium or zinc-containing actives. In parenteral nutrition, lactic acid is used less often than citric or acetic acid, but it appears in a narrow set of sterile solutions where its metabolism to pyruvate is acceptable. Any use in injectable products must be supported by bacterial endotoxin release testing by Ph. Eur. 2.6.14 or USP <85>, because the route of administration makes endotoxin compliance non-negotiable.

    In haemodialysis and peritoneal dialysis, L(+)-lactic acid serves as an acidifying agent and bicarbonate precursor in acidified concentrate formulations. The acidified concentrate is held at pH 2.8–3.5 to prevent precipitation of calcium carbonate and magnesium carbonate during storage, then proportioned with bicarbonate concentrate in the dialysis machine. Final dialysate lactate concentrations commonly range from 35 to 40 mmol/L, which corresponds to a lactic acid concentration in the liquid concentrate depending on the dilution ratio; a 1:32.775 proportioning system requires a lactic acid concentrate concentration near 1.1–1.3 mol/L. Ultrapure dialysate is specified to an endotoxin level of ≤ 0.03 EU/mL, so the incoming pharmaceutical grade lactic acid must contribute negligible endotoxin after dilution. Technical or food grade lactic acid with uncontrolled endotoxin can overload the final dialyser and trigger an inflammatory response; therefore substitution is not acceptable without a documented ultrafiltration and endotoxin-reduction step.

    In absorbable polymer synthesis, pharmaceutical grade lactic acid is the monomer source for lactide and, after dimerisation, for poly(L-lactic acid) and poly(lactic-co-glycolic acid). Ring-opening polymerisation with stannous octoate catalyst requires an L-isomer content exceeding 99.0% for semi-crystalline PLLA; the D-isomer threshold of ≤ 2.5% in the 90% pharmaceutical solution is only a starting point. If technical grade lactic acid with D-isomer > 5% is used, the resulting polymer shows depressed melting point, reduced crystallinity, and faster hydrolytic degradation, which alters drug-release kinetics in PLGA microsphere products. Metal impurities such as iron, aluminium, and tin are also limited to prevent catalyst deactivation and polymer discolouration. In this application, the document trail matters as much as the chemical profile: batch-to-batch variance in residual sugars or sulfated ash changes lactide yield and optical rotation, so pharmaceutical grade material is used under change control.

    Operational boundaries are defined by the corrosive and hygroscopic nature of the material. It is incompatible with strong oxidisers, concentrated mineral acids, aluminium, and carbon steel; neutralisation with amines or alkali carbonates is strongly exothermic and must be cooled. Storage is recommended at 15–25 °C in tightly closed, nitrogen-flushed containers; repeated exposure to air above 60% RH increases water content and oligomer equilibration, and prolonged storage above 40 °C can discolour the solution and increase lactide formation. If the material is frozen, thawing may produce temporary stratification; bulk tanks should be recirculated before sampling to ensure a representative release sample. These limits are not marketing statements; they are derived from the same specifications that pharmaceutical manufacturers audit under excipient supplier qualification.

    Distinction Between Pharmaceutical, Food, and Technical Lactic Acid Grades

    Total acidity alone cannot differentiate pharmaceutical grade from food or technical material. Two drums each marked 90% lactic acid can differ by orders of magnitude in endotoxin, heavy metal, residual solvent, and microbial load. Food grade lactic acid certified to FCC or JECFA is suitable for acidification of fermented meat, dairy products, and confectionery, but it is not tested for bacterial endotoxins and often allows higher total aerobic microbial count. Technical grade lactic acid is a commodity product used in metal cleaning, oilfield stimulation, textile mordanting, and industrial neutralisation; it may contain residual reducing sugars, sulfated ash, and colour bodies that require distillation, ion exchange, or carbon treatment before pharmaceutical consideration. Reagent grade lactic acid may meet assay and titration specifications but is generally not tested for endotoxin, particulate matter, or residual solvents under pharmaceutical conditions.

    Typical grade differentiation for aqueous lactic acid solutions
    PropertyPharmaceutical gradeFood gradeTechnical grade
    Total acidity88.0–92.0% w/w80.0–88.0% w/w or declared50.0–80.0% w/w variable
    Stereochemical purityL ≥ 97.5%L ≥ 95% if declareduncontrolled
    Bacterial endotoxins≤ 0.25 EU/mgnot controllednot controlled
    Heavy metalsICH Q3D / ≤ 5 ppm as Pb≤ 10 ppm as Pbnot controlled or ≤ 50 ppm
    Residual solventsClass 3 controlled; methanol ≤ 50 ppmlimited if solvent process usednot controlled
    Microbial limitsTAMC ≤ 100 CFU/g, TYMC ≤ 10 CFU/gTAMC ≤ 1,000 CFU/gnot specified
    Primary useparenteral excipient, dialysis, API intermediateacidulant, preservative, food pH controlmetal cleaning, oilfield, textile, industrial neutralisation

    When a manufacturer considers replacing pharmaceutical grade with food or technical material, the excipient risk assessment must address the route of administration, the presence of D-lactic acid, endotoxin, elemental impurities under ICH Q3D, residual solvent class limits under Ph. Eur. 2.4.24 or USP <467>, and microbial quality under Ph. Eur. 2.6.12/2.6.13 or USP <61>. Process validation batches must be repeated against USP <85>, USP <232>/<233>, and USP <467> before release. Food grade lactic acid can serve as a starting material for pharmaceutical grade after additional purification, but it must be re-qualified, not simply relabelled. This grade distinction, rather than the nominal acid concentration, is the principal specification that purchasing and quality units must control.