| HS Code | 666099 |
| Chemical Name | DL-Isoleucine |
| Iupac Name | 2-amino-3-methylpentanoic acid |
| Cas Number | 443-79-8 |
| Molecular Formula | C6H13NO2 |
| Molecular Weight | 131.17 g/mol |
| Appearance | White crystalline powder |
| Melting Point | 292°C (decomposes) |
| Solubility | Soluble in water (approx. 41 g/L at 20°C); soluble in dilute acids and alkalis; slightly soluble in ethanol |
| Density | 1.17 g/cm³ (calculated) |
| Pka | 2.36 (carboxyl), 9.60 (amino) |
| Optical Rotation | [α]D = 0° (racemic mixture, in water) |
| Exact Mass | 131.0946 g/mol |
| Hydrogen Bond Donor Count | 2 |
| Hydrogen Bond Acceptor Count | 3 |
| Storage Conditions | Store in a cool, dry, sealed container; avoid light and moisture |
| Typical Purity | ≥98% |
As an accredited DL-isoleucine factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | DL-isoleucine is supplied in 25 kg fiber drums with double polyethylene liners, sealed and clearly labeled. |
| Container Loading (20′ FCL) | DL-isoleucine shipped in 20′ FCL as full container load, packed in sealed drums, moisture-proof, stable non-hazardous chemical. |
| Shipping | DL-isoleucine ships as a non-hazardous amino acid powder in sealed, moisture-resistant containers. Store at ambient temperature, away from heat and humidity. Ensure proper labeling and documentation for customs. No special transport restrictions apply, though avoid excessive pressure and prolonged exposure to sunlight during transit. |
| Storage | Store DL-isoleucine in a tightly sealed container in a cool, dry, well-ventilated area. Protect from moisture, direct sunlight, and extreme heat. Keep away from strong oxidizing agents and incompatible substances. Ensure the container is clearly labeled and inaccessible to unauthorized personnel. Refrigeration is generally unnecessary; maintain stable room temperature conditions for optimal stability. |
| Shelf Life | DL-isoleucine has a typical shelf life of 2–3 years when stored unopened in a cool, dry, airtight container away from light. |
In low-crude-protein broiler and swine formulations, DL-isoleucine is evaluated as a racemic source of standardised ileal digestible isoleucine rather than as a mass-for-mass replacement for L-isoleucine. The complete feed matrix is formulated against standardized ileal digestible isoleucine targets expressed on a dry matter basis, commonly 0.40% to 0.78% depending on species and production phase. The supplemental contribution is calculated by subtracting native isoleucine originating from corn, soybean meal, and byproduct protein sources. Regulatory acceptance in the European Union requires that the material be identified under Regulation (EC) No 1831/2003 where it is placed on the market as a nutritional feed additive, and batch documentation is aligned with FAMI-QS Code of Practice version 6.0. Release testing follows ISO 13903:2005 for amino acid determination and AOAC Method 994.12 for feed hydrolysate analysis. Because DL-isoleucine contains approximately 50% L-isoleucine and 50% D-isoleucine, inclusion mass is corrected on an active L-isoleucine basis. Published in vivo bioequivalence data for D-isoleucine in broilers and weaned pigs are limited, so feed mills routinely validate standardized ileal digestible isoleucine response over a 7- to 14-day performance flush before the final formula is locked.
Typical DL-isoleucine inclusion for broiler grower diets formulated at reduced crude protein is 0.5 to 1.6 kg per metric tonne, while swine grower-finisher diets may require 0.3 to 0.9 kg per metric tonne. In extruded aquafeed, 0.4 to 1.2 kg per metric tonne is used only after digestibility screening because fish and shrimp responses to the D-isomer are species-dependent. The downstream production sequence begins with a microingredient premix in a ribbon blender where DL-isoleucine is dispersed on a wheat middlings or rice hull carrier for 15 to 20 minutes until an in-house coefficient of variation below 5% is achieved. The premix is then transferred to the main mixer and combined with macroingredients before conditioning at 75°C to 85°C for 30 to 60 seconds and pelleting. When the complete feed contains reducing sugars or high-moisture byproducts, conditioning temperature is reduced by 5°C to 10°C to limit Maillard product formation. Terminal products include pelleted broiler finishing feed, meal or pelleted swine grower-finisher feed, and extruded aquaculture pellets.
| Species and production phase | Standardized ileal digestible isoleucine target (% dry matter) | DL-isoleucine inclusion mass (kg/tonne) | Release analytical method |
|---|---|---|---|
| Broiler starter | 0.72–0.78 | 0.8–1.6 | ISO 13903:2005, AOAC 994.12 |
| Broiler grower-finisher | 0.60–0.68 | 0.5–1.3 | ISO 13903:2005 |
| Swine nursery | 0.55–0.62 | 0.6–1.4 | ISO 13903:2005 |
| Swine grower-finisher | 0.40–0.48 | 0.3–0.9 | AOAC 994.12 |
| Aquaculture extruded feed | 0.50–0.60 | 0.4–1.2 | ISO 13903:2005 |
Substitution of L-isoleucine with the racemic mixture in animal cell culture is not a mass-for-mass replacement. Mammalian cell lines such as Chinese hamster ovary cells and Vero cells exhibit stereospecific transport and metabolic flux through branched-chain amino acid catabolism; the D-isoleucine fraction is generally not a substrate for branched-chain aminotransferase and may compete for the L-type amino acid transporter at elevated concentration. For this reason DL-isoleucine is confined to ancillary-media and non-clinical process development applications unless the D-isoleucine fraction is removed before cell contact. Regulatory alignment for material used in biopharmaceutical manufacturing includes documentation under the principles of ICH Q5A and ICH Q5D, evaluation as an ancillary material under USP <1043>, and sterility testing according to USP <71> where applicable. Basal chemically defined media are typically formulated to provide L-isoleucine in the range of 0.4 to 0.8 mM. If DL-isoleucine is used as a development substitute, the total racemate concentration is adjusted to 0.8 to 1.6 mM to deliver equivalent L-isoleucine, and a no-observed-effect screen is performed in the host cell line because published DL-isoleucine cytotoxicity thresholds for Chinese hamster ovary cell cultures are limited.
Downstream dry powder media production involving DL-isoleucine is executed in low-humidity suites maintained below 40% relative humidity with nitrogen-purged blending to prevent agglomeration and oxidative degradation of adjacent amino acids. The powder is milled through a pin mill and blended with salts, vitamins, and trace elements. The complete dry powder is then reconstituted and sterile-filtered through a 0.22 µm membrane before liquid-media filling. Liquid fed-batch supplement concentrates are prepared at 10× to 20× concentration and stored at 2°C to 8°C; addition to the bioreactor is controlled by linked pH and dissolved-oxygen loops. Terminal products include Chinese hamster ovary cell-produced monoclonal antibodies, recombinant coagulation factors, viral vaccines produced on Vero cells, and process development media for cell bank expansion.
DL-Isoleucine is handled as a protected amino acid building block in solution-phase and solid-phase peptide synthesis when racemic material is deliberately introduced to probe coupling efficiency or to generate diastereomeric intermediates for chromatographic separation. The carboxyl group is activated with N,N′-diisopropylcarbodiimide in the presence of 1-hydroxybenzotriazole in aprotic dimethylformamide at 0°C to 5°C to minimise oxazolone formation and racemization. Coupling is performed with 1.0 to 1.2 molar equivalents of DL-isoleucine relative to the amino-terminal peptide component. When Fmoc protection is used, piperidine-mediated deprotection in dimethylformamide is monitored by ultraviolet absorbance at 301 nm; when Boc protection is used, trifluoroacetic acid cleavage in dichloromethane is followed by cold diethyl ether precipitation. Regulatory compliance for material supplied as an active pharmaceutical ingredient intermediate follows ICH Q7 for GMP starting materials, REACH Regulation (EC) No 1907/2006 for EU import, and USP <731> loss on drying or USP <921> water determination where certificate of analysis includes residual solvent data.
Because racemic isoleucine yields diastereomeric peptides when coupled to enantiopure sequences, preparative reverse-phase C18 high-performance liquid chromatography with acetonitrile and 0.1% trifluoroacetic acid gradients is used to resolve the resulting diastereomers. Terminal product classes include N-protected DL-isoleucine derivatives, racemic peptide standards used for impurity profiling, and non-receptor-binding peptide intermediates for later chiral separation. For stereospecific peptide active pharmaceutical ingredients, DL-isoleucine is not introduced into the final sequence; instead the material is resolved to L-isoleucine before final coupling, and the remaining D-isoleucine stream is recovered or returned as a racemization feedstock.
During post-emulsification cooling in personal care manufacturing, DL-isoleucine is added as a water-phase conditioning agent after the oil-in-water emulsion has been formed and the bulk temperature has dropped to 35°C to 40°C. The addition ratio ranges from 0.1 to 2.0 wt% in leave-on facial emulsions and 0.05 to 0.5 wt% in rinse-off hair conditioners. The powder is pre-dispersed in demineralized water and glycerin at a 1:10 solid-to-liquid ratio before introduction under a low-shear anchor stirrer. The formula is adjusted to pH 4.8 to 5.5 with citric acid to maintain the amino acid′s zwitterionic charge density and to prevent acid-catalyzed hydrolysis of ester-based emollients. Cosmetic products containing DL-isoleucine are assessed according to Regulation (EC) No 1223/2009, ISO 11930:2019 preservation challenge testing, and ISO 16128-1:2016 natural-origin index accounting where applicable. Terminal products include hair conditioning rinses, scalp treatment lotions, and facial moisturizing emulsions.
Amino acid analyzer calibration and system suitability testing require racemic isoleucine as a retention-time marker because the chromatographic resolution of D-isoleucine, L-isoleucine, L-allo-isoleucine, and leucine on sulfonated polystyrene cation-exchange columns is a recognized indicator of column performance. Working calibration standards are prepared gravimetrically in 0.1 M hydrochloric acid to a concentration of 0.05 to 2.0 µmol/mL, then diluted in lithium citrate loading buffer at pH 2.2 and injected at a nominal volume of 50 µL. The analytical sequence uses post-column ninhydrin derivatization at 135°C with dual-channel photometric detection at 440 nm and 570 nm. Results are processed under ISO/IEC 17025:2017 general competence requirements, and reference material producers operate under ISO 17034:2016 to assign purity and expanded uncertainty. Terminal products include certified amino acid reference standard kits, system suitability test mixtures, and quality-control solutions for feed and food testing laboratories.
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For preparative chemistry and media development groups that require a defined racemic branched-chain amino acid, DL-isoleucine is supplied as a white to off-white crystalline powder with CAS registry number 443-79-8, molecular formula C6H13NO2, and relative molecular mass 131.17 g mol⁻¹. The term DL-isoleucine denotes a 1:1 racemic mixture of D-isoleucine and L-isoleucine, and does not include the diastereomeric D-alloisoleucine and L-alloisoleucine unless separately declared. Commercial grade designations include reagent grade, biochemical grade, and amino acid analyzer calibration grade; the specific catalogue model is manufacturer-dependent. Release specifications for a reagent-grade material generally contain assay by non-aqueous titration with 0.1 mol L⁻¹ perchloric acid between 98.5% and 101.5% on the dried basis, loss on drying not more than 0.20% by USP <731>, residue on ignition not more than 0.10% by USP <281>, chloride not more than 0.020%, sulfate not more than 0.020%, iron not more than 0.001%, and heavy metals not more than 0.001% by USP <231> or an equivalent limit. Identification is confirmed by infrared absorption against a reference spectrum using a potassium bromide disc in an FTIR spectrophotometer; the carboxylate and ammonium deformation bands in the region near 1600 cm⁻¹ and 1500 cm⁻¹ are diagnostic. Optical quality is monitored by polarimetry at 589 nm using a 100 mm cell and a solution concentration of 40 g L⁻¹ in 6 mol L⁻¹ HCl; acceptance is normally −0.5° to +0.5° for the racemate, whereas significant deviations indicate enantiomeric enrichment or contamination by a chiral impurity.
Chemical synthesis of DL-isoleucine via a Strecker condensation of 2-methylbutanal with sodium cyanide and ammonium chloride, followed by acid hydrolysis, yields a mixture of stereoisomers because both the α-carbon and β-carbon centers are formed under non-stereoselective conditions. Industrial isolation of DL-isoleucine therefore requires crystallization protocols that exclude the allo diastereomers by solubility difference or chromatographic separation; the racemic product is crystalline but is not a single chiral entity. The Strecker route is contrasted with a fermentative route for L-isoleucine, which is produced by Corynebacterium glutamicum strains under aerobic fed-batch conditions and is subsequently isolated as the single enantiomer by ion-exchange chromatography or crystallization. Published quantitative process yields for specific production strains are limited, but the racemic material is generally lower cost only when downstream chiral resolution is unnecessary or when the racemate itself is the required reference material.
Because only the L-enantiomer is aminoacylated by eukaryotic aminoacyl-tRNA synthetases and incorporated into polypeptide chains, the racemate cannot be regarded as a metabolically equivalent drop-in for L-isoleucine in mammalian cell culture or monogastric nutrition. In a chemically defined medium designed for Chinese hamster ovary cells, substitution of L-isoleucine by DL-isoleucine on an equal-mass basis delivers only approximately 50% biologically available L-isoleucine if the cell line lacks D-amino acid oxidase or racemase activity; published data for specific cell lines are limited, and dose verification should be performed with spent-media amino acid analysis by ion-exchange chromatography with post-column ninhydrin detection according to ISO 13903:2005 or an equivalent validated method. The D-enantiomer may compete for amino acid transport at the sodium-independent system L carrier, but transport kinetics are stereoselective and variable across species and tissue origin. Where a fermentation process uses a bacterial auxotroph that requires L-isoleucine, the racemate is typically screened only after chiral purity and D-isoleucine content are controlled, because the biologically relevant concentration of L-isoleucine is one-half of the added mass.
In solid-phase peptide synthesis, the use of DL-isoleucine as a raw material is generally restricted to preparation of racemic standards or structure-activity relationship studies. Preparation of N-protected derivatives such as N-tert-butoxycarbonyl-DL-isoleucine is undertaken under Schotten-Baumann conditions with pH maintained between 9.0 and 10.5 using a pH-stat and sodium hydroxide. Coupling of the racemate in solid-phase synthesis produces diastereomeric peptides that must be resolved by reversed-phase HPLC with a C18 column and an acetonitrile/ammonium formate gradient; under these conditions the L-isoleucyl and D-isoleucyl peptides may co-elute unless a chiral column is used. Laboratories performing chiral purity verification commonly derivatize with ortho-phthaldialdehyde plus N-isobutyryl-L-cysteine and separate the resulting diastereomeric isoindoles on a C18 column with fluorescence detection at excitation 340 nm and emission 450 nm. Sub-percent detection is attainable with careful mobile-phase optimization, but the limit of quantitation must be established for each detector and column configuration.
Enzyme-mediated resolution of DL-isoleucine begins with acetylation of the racemate using acetic anhydride under alkaline pH. N-acetyl-DL-isoleucine is then subjected to acylase I from porcine kidney at pH 7.5 and 37 °C. The reaction selectively deacetylates the L-enantiomer, producing free L-isoleucine and N-acetyl-D-isoleucine; the two products are separated by precipitation or cation-exchange chromatography. This route is used when a process requires enantiopure L-isoleucine from the racemate; the residual N-acetyl-D-isoleucine may be racemized under acetic anhydride conditions and recycled. Kinetic parameters such as conversion at 4 h are enzyme-lot dependent; therefore, design-of-experiment studies in a stirred reaction calorimeter are required before scale-up.
In bacterial fermentation, DL-isoleucine is often added as a solid before heat sterilization or as a sterile-filtered solution after autoclaving. Solubility in water is pH dependent; below the carboxyl pKa of approximately 2.36 the cationic form predominates, and above the amino pKa of approximately 9.68 the anionic form dominates, both of which increase solubility relative to the zwitterionic form near pH 5.5–6.5. A concentrated stock solution prepared at 20 g L⁻¹ may remain partly undissolved in the zwitterionic range; complete dissolution should be confirmed in a controlled-temperature vessel at 25 °C with a 0.45 µm membrane filtration step before aseptic addition. Heat sterilization at 121 °C for 15 min in the presence of reducing sugars can induce Maillard-derived browning and reduce available amino nitrogen; therefore, the amino acid is preferably sterilized separately or added after the carbohydrate solution has cooled to below 80 °C.
| Parameter | Typical acceptance limit | Method or equipment |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual inspection |
| Identification | Infrared spectrum matches reference | FTIR, KBr disc |
| Assay, dried basis | 98.5%–101.5% | Non-aqueous titration with 0.1 mol L⁻¹ HClO₄ |
| Specific rotation | −0.5° to +0.5° | Polarimeter, c = 4, 6 mol L⁻¹ HCl, 589 nm |
| Loss on drying | ≤0.20% | USP <731> |
| Residue on ignition | ≤0.10% | USP <281> |
| Chloride | ≤0.020% | USP <221> |
| Sulfate | ≤0.020% | USP <221> |
| Iron | ≤0.001% | USP <241> |
| Heavy metals | ≤0.001% | USP <231> or equivalent |
| Total aerobic microbial count | ≤103 CFU g⁻¹ | USP <61> |
| Moulds and yeasts | ≤102 CFU g⁻¹ | USP <61> |
In dry blending of amino acid premixes, batch-to-batch variance in tapped bulk density and particle size distribution affects segregation in a double-cone blender. A typical specification may require 95% passage through a 60 mesh sieve and tapped bulk density between 0.35 g cm⁻³ and 0.65 g cm⁻³; the exact range must be taken from the supplier certificate because the material is not a directly fluid-bed granulated product. Segregation can be minimized by using a bin blender with a fill volume between 50% and 70% and an intensifier bar speed below 150 rpm, but the acceptable operating envelope is equipment-specific. When DL-isoleucine is blended with L-isoleucine, L-valine, and L-leucine for branched-chain amino acid analysis standards, the blend should be assayed by HPLC after derivatization to confirm the nominal content because hygroscopic caking can cause local agglomerates. Storage in low-density polyethylene bags inside sealed aluminium-lined drums at 20–25 °C and relative humidity below 40% is recommended; exposure to high humidity increases caking without necessarily increasing loss on drying above 0.2%.
Solution preparation for continuous chromatography or bioconversion should account for the zwitterionic equilibrium. At a temperature of 25 °C, a racemate suspension in water generates a conductivity that is dominated by the partial dissociation of the carboxyl and ammonium groups; pH adjustment with 1 mol L⁻¹ hydrochloric acid to pH 2.0 or with 1 mol L⁻¹ sodium hydroxide to pH 9.5 increases dissolved fraction and reduces the need for extended mixing. A jacketed stirred vessel with a retreat-curve impeller operating at 150–250 rpm provides adequate dispersion for laboratory-scale preparation up to 100 L. Filtration through a 0.22 µm polyethersulfone membrane is used when the solution is to be transferred into a bioreactor; membrane fouling is lower when the pH is held below 3.0 or above 9.0 because the zwitterionic precipitate is minimized. Published data for specific solubility maxima in binary water-ethanol or water-acetone systems are limited; process development groups are advised to generate solubility curves by gravimetric method using a thermostatic shaker bath and 0.45 µm syringe filtration before scaling to production.
For analytical reference work, the principal differences are not cosmetic but are defined by stereochemistry and optical rotation. L-Isoleucine has CAS registry number 73-32-5 and is the proteinogenic branched-chain amino acid found in mammalian proteins; D-Isoleucine has CAS registry number 319-78-8 and is its mirror image; DL-isoleucine is the racemic mixture with CAS registry number 443-79-8. L-Alloisoleucine is a diastereomer of L-isoleucine that appears in plasma during maple syrup urine disease and is resolved by the same OPA chiral-thiol derivatization protocols. In cation-exchange amino acid analysis, L-isoleucine and L-alloisoleucine are separated under optimized lithium buffer gradients at column temperatures between 30 °C and 70 °C; the racemate cannot be used as a single reference for that separation because it contains only the isoleucine enantiomers and not necessarily the allo forms.
| Attribute | DL-Isoleucine | L-Isoleucine | D-Isoleucine | L-Alloisoleucine |
|---|---|---|---|---|
| CAS registry number | 443-79-8 | 73-32-5 | 319-78-8 | 1509-34-8 |
| Stereochemical relation | Racemic mixture of D- and L-isoleucine | Proteinogenic enantiomer | Mirror image of L-isoleucine | Diastereomer of L-isoleucine |
| Optical rotation | Near zero | Positive | Negative | Distinct from L-isoleucine |
| Protein incorporation | One-half available as L-isoleucine in absence of racemase | Fully available in eukaryotic systems | Not incorporated by eukaryotic aminoacyl-tRNA synthetases | Not a normal proteinogenic constituent |
| Primary use | Chiral reference, synthesis intermediate | Cell culture, nutrition, fermentation | Enzyme specificity studies | Metabolic disease marker |