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Feed Grade Valine

    Specifications
    HS Code 310591
    Product Name Feed Grade Valine
    Chemical Name L-Valine
    Chemical Formula C5H11NO2
    Molecular Weight 117.15 g/mol
    Cas Number 72-18-4
    Appearance white crystalline powder
    Assay 98.5% min
    Loss On Drying 0.5% max
    Heavy Metals 10 mg/kg max
    Arsenic 2 mg/kg max
    Lead 10 mg/kg max
    Cadmium 1 mg/kg max
    Mercury 0.1 mg/kg max
    Total Plate Count 1000 CFU/g max
    Salmonella negative in 25 g
    Solubility soluble in water, slightly soluble in ethanol
    Ph 5.5 to 7.0 (1% aqueous solution)

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

    Packing & Storage
    Packing Feed Grade Valine is packaged in 25 kg multilayer paper-plastic bags, sealed to protect against moisture and contamination.
    Container Loading (20′ FCL) Loading 20,000kg of Feed Grade Valine in 20kg bags on pallets, secured for 20′ FCL shipment.
    Shipping Feed Grade Valine ships as a free-flowing powder in multi-layer kraft bags or bulk containers. Keep dry, sealed, and away from heat sources. Ensure proper labeling for non-hazardous cargo. Avoid contamination with toxic substances. Transportation is safe under standard conditions; store in ventilated area.
    Storage Store Feed Grade Valine in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed to prevent caking or contamination. Avoid contact with strong oxidizers and acids. Maintain good hygiene and use appropriate handling equipment. Under proper storage conditions, shelf life is typically 24 months from manufacture date.
    Shelf Life Shelf life is typically 2-3 years when stored in a cool, dry, well-ventilated area away from moisture and direct sunlight.
    Application of Feed Grade Valine

    In post-weaning Phase 2 diets with 21–23% crude protein and 1.25–1.30% standardized ileal digestible lysine, feed-grade L-valine 98.5% is added at 0.65–1.10 kg/t to move the SID Val:Lys ratio from a corn–soybean meal basal in the range of 0.58–0.63 toward 0.67–0.70. The European Union route for this ingredient is anchored in Regulation (EC) No 1831/2003, Annex I, category 3c, covering amino acids and their salts as nutritional feed additives; batch release and dispute testing are performed by ISO 13903:2005 after acid hydrolysis, with AOAC 994.12 used as a referee method in third-party certificates. Because crystalline L-valine has a different bulk density than ground corn and soybean meal, the additive is pre-blended with ground corn carrier at a mass ratio between 1:4 and 1:8 before entry into the twin-shaft paddle mixer. Addition order places the diluted valine premix after trace minerals and choline chloride but before soybean meal and whey permeate; post-mix HPLC analysis normally requires a coefficient of variation below 5% for valine recovery. The downstream crumble line uses a hammer-mill screen of 2.5–3.0 mm, steam conditioning at 75–82°C for 45–60 s, and a 2.5 mm die with compression ratio 4.0–4.5:1. Crumbler roll gap is held at 1.8–2.2 mm to control fines. Terminal product types are weaner prestarter crumbles and 2.5 mm nursery pellets with 12–15% lactose contributed by whey permeate.

    At What Digestible Valine:Lysine Ratio Does Breast Meat Yield Plateau in Low-Protein Broiler Starter Feeds?

    Broiler starter feeds formulated to 1.22–1.28% digestible lysine and 21.5–22.5% crude protein require 0.55–0.95 kg/t feed-grade L-valine 98% to raise digestible Val:Lys from the unsupplemented 0.65–0.69 band into the 0.76–0.80 plateau associated with breast muscle deposition. The exact plateau is diet-dependent: wheat-based pre-starters with 20–25% wheat inclusion typically push the addition toward the upper end because the available valine contribution from wheat-containing basal feeds differs from that of corn–soybean meal systems. EU market documentation cites Regulation (EC) No 1831/2003, Annex I, category 3c for the nutritional additive classification, while shipment release relies on ISO 13903:2005 quantification and AOAC 994.12 verification. In the mill, corn and soybean meal are ground through a 1.5–2.0 mm screen, conditioned at 85–88°C for 75–90 s, and pressed through a 2.5–3.0 mm die at compression ratio 5.0:1 before crumbling between rolls set at 1.5–2.0 mm. A process threshold exists when cane molasses exceeds 4% and conditioning time exceeds 120 s at 88°C; under those conditions, Maillard adduct formation on free amino groups can reduce free valine recovery and darken the crumble. The terminal products are steam-crumbled broiler prestarter and starter feeds at 22–23% crude protein.

    Thermal Stability Window for Free Amino Acids in Extruded Salmonid Feeds

    Extruded rainbow trout grower rations containing 120–150 g/kg fishmeal and 22–26% total lipid are supplemented with 0.8–1.6 kg/t feed-grade L-valine to hold apparent Val:Lys at 0.75–0.78 after fishmeal reduction. This application is covered in EU feed law by Regulation (EC) No 1831/2003, Annex I, category 3c; routine release testing is conducted under ISO 13903:2005, with AOAC 994.12 as the referee method. The production line is configured around a twin-screw extruder with L/D 24:1 and a screw profile generating 190–220 Wh/kg specific mechanical energy. Pre-conditioning runs at 90–95°C with 28–30% moisture, followed by a die plate of 2.0 mm with open area between 0.8 mm² and 1.2 mm². Since crystalline L-valine has water solubility of approximately 85 g/L at 25°C, preconditioner condensate accumulation is controlled by holding discharge moisture at ≤25% before the extruder barrel; this prevents free amino acid migration toward the pellet surface. Post-extrusion vacuum coating at 0.8 bar applies 12–18% fish oil onto the pellet matrix. Terminal product types are extruded sinking grower pellets 2–4 mm in diameter at 8–10% final moisture.

    When Fishmeal Drops Below 120 g/kg in Vannamei Shrimp Formulations

    Reduction of fishmeal below 120 g/kg in Litopenaeus vannamei grow-out formulations creates a crystalline valine requirement of 0.7–1.3 kg/t because plant protein sources such as soybean meal and pea protein concentrate supply a marginal branched-chain amino acid balance. The target apparent Val:Lys is held between 0.72 and 0.78 in a 35–38% crude protein diet. EU import documentation references Regulation (EC) No 1831/2003, Annex I, category 3c, and analytical release is performed by ISO 13903:2005, with AOAC 994.12 certificates required by some Southeast Asian feed-mill procurement specifications. The production sequence starts with micro-grinding to a median particle size of 0.25–0.35 mm, followed by incorporation of pregelatinized tapioca starch at 8–12% as a leaching-control binder. Conditioning at 90–95°C with 10–14% added water precedes a 1.5–2.0 mm pellet die, and the formed pellets enter post-conditioning at 90°C for 15–20 min before drying at 60–70°C to 8–10% moisture. Post-curing is necessary because L-valine is water-soluble; uncured micro-pellets release free valine into the pond water during immersion, while cured crumbles retain nutrient integrity during the prolonged feeding interval typical of shrimp. Terminal product types are 1.2–2.2 mm shrimp crumbles and micro-pellets.

    Late-Gestation and Lactation Sow Diets Do Not Metabolize Valine Like Growing Pig Diets

    Lactation formulations for hyperprolific sows typically require a smaller feed-grade L-valine addition than nursery feeds: 0.4–0.8 kg/t is used to maintain SID Val:Lys at 0.72–0.74 against a SID lysine specification of 0.80–0.85%. Published dose-response data for this specific configuration is limited, so purchase and formulation decisions rely on total amino acid verification by ISO 13903:2005 rather than an independent valine response model. The EU regulatory classification is Regulation (EC) No 1831/2003, Annex I, category 3c, and AOAC 994.12 is used in third-party certificates. On the production side, sow feeds pass through a hammer-mill screen of 4.0–5.0 mm, receive steam conditioning at 70–75°C for 30–45 s, and are pressed through a 4.5–5.0 mm die at compression ratio 3.5:1. Finished product types are lactation mash or 4.5 mm pellets at 15–17% crude protein.

    Layer phase 4 mashes with 14.5–15.5% crude protein and 0.70–0.75% digestible lysine are supplemented with 0.3–0.7 kg/t feed-grade L-valine 98.5% to support late-cycle egg mass when methionine and lysine are already optimized. In this low-protein layer context, the digestible Val:Lys target is kept between 0.78 and 0.82 because albumen synthesis places continuous demand on plasma valine after peak production. The EU feed-additive classification under Regulation (EC) No 1831/2003, Annex I, category 3c applies, with ISO 13903:2005 as the primary release method and AOAC 994.12 for verification. Unlike broiler crumble lines, layer operations frequently retain a high proportion of mash; the valine premix is added after calcium carbonate and before oil so that electrostatic adhesion to limestone particles does not depress analytical recovery. Primary milling uses a 6.0 mm roller-mill or hammer-mill screen. Final products are complete layer meal or 4.0 mm low-temperature pellets conditioned at 70–75°C, without post-cooking. Terminal product types are complete layer mashes and 4.0 mm pellets for cage-free and enriched colony housing systems.

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    Certification & Compliance
    More Introduction

    Feed-grade L-valine is produced by aerobic submerged fermentation using selected strains of Corynebacterium glutamicum or Escherichia coli K-12 derivatives, followed by ion-exchange separation, activated carbon decolorization, crystallization, drying, and sieving to a controlled particle size. The product is designated chemically as (2S)-2-amino-3-methylbutanoic acid, CAS 72-18-4, empirical formula C5H11NO2, and molecular mass 117.15 g/mol. Commercial feed additive models appear as L-Valine 98 or L-Valine 98.5 feed grade, in which the numerical designation refers to mass fraction of L-valine on a dry matter basis. As a neutral, aliphatic, branched-chain amino acid, L-valine is not synthesized by monogastric animals at a rate that meets requirements for skeletal muscle protein accretion, milk protein output, or immune cell proliferation; dietary supply is therefore obligatory. Certified lot release documentation for this material normally covers assay, moisture content, residue on ignition, optical rotation, and elemental impurities.

    The term “feed grade” distinguishes this material from pharmaceutical or food-grade L-valine, primarily through microbial and heavy metal limits and through the absence of excipient-grade dust control additives. Feed additive registration under national regulations may require a quantitative declaration of the active substance, a statement of the manufacturing strain, and lot-level certificates of analysis for heavy metals, arsenic, and microbial load. In export transactions, model codes include the base designation “Valine Feed Grade” plus a supplier site identifier and a lot-specific traceability sequence; these codes are not internationally standardized and require verification against the local feed additive register.

    What Distinguishes Feed-Grade Valine from Lysine, Methionine, and Other Supplementary Amino Acids?

    The structural distinction is the branched aliphatic side chain, which places L-valine with L-leucine and L-isoleucine in the branched-chain amino acid family. In feed-grade crystalline form, L-valine is a free amino acid, unlike the principal commercial form of lysine, which is L-lysine monohydrochloride containing 78.8 g/100 g free lysine. The absence of chloride removes any effect on dietary electrolyte balance and allows valine supplementation without shifting the dietary cation-anion ratio. Methionine is sold predominantly as DL-methionine, a racemic mixture requiring conversion of the D-isomer to the L-isomer by the animal before protein synthesis; L-valine feed grade is already the biologically active L-isomer. Threonine and tryptophan introduce hydroxyl and indole side chains, respectively, and participate in different gut mucosal oxidation and serotonin precursor pathways; valine does not carry these functional groups.

    In practical corn–soybean meal formulations, the more operationally important difference is limiting order. L-lysine, DL-methionine, L-threonine, and L-tryptophan are usually supplemented first because they become limiting before valine. When total crude protein is reduced by 2–4 percentage points by removing soybean meal, valine commonly becomes the next limiting amino acid in growing pigs and broilers. Branched-chain amino acids share leucine-preferring transport systems and the rate-limiting enzyme complex branched-chain α-keto acid dehydrogenase. Excess dietary leucine from blood meal, corn gluten meal, or over-supplementation can upregulate oxidative decarboxylation of all three branched-chain amino acids and can precipitate a valine deficiency even when total dietary valine appears adequate. In such cases, a margin of 5–10% above the minimum standardized ileal digestible valine-to-lysine ratio is used in field formulations; published dose-response slopes for this interaction are limited.

    Because L-valine is a branched-chain amino acid, it shares absorptive and metabolic pathways with leucine and isoleucine. In enterocyte and skeletal muscle membrane transport, system L and system B0 carriers transport large neutral amino acids; leucine and valine can compete for sodium-independent transport capacity. This is not an issue with lysine, which is transported by system y+ for cationic amino acids, or with methionine, which is transported by sodium-dependent neutral amino acid systems. The practical consequence is that high leucine inclusion from corn coproducts can reduce apparent valine utilization; therefore, formulators using distillers dried grains with solubles often increase the standardized ileal digestible valine-to-lysine ratio by 3–7% relative to corn–soybean meal controls.

    AdditiveFeed-grade product formActive moiety mass fractionMain structural or functional distinction
    L-LysineL-lysine monohydrochloride78.8 g/100 g lysineChloride counterion; cationic amino acid transport
    DL-MethionineRacemic crystals99 g/100 g methionineRequires D-to-L conversion for protein synthesis
    L-ThreonineCrystalline feed grade98.5 g/100 g threonineHydroxyl side chain; gut mucosal substrate
    L-TryptophanCrystalline feed grade98.5 g/100 g tryptophanIndole side chain; serotonin precursor
    L-ValineCrystalline feed grade98.5 g/100 g valineBranched-chain aliphatic side chain; no counterion

    Release Specification Profile and Analytical Reference Methods

    The following table summarizes typical release limits drawn from supplier certificates of analysis for feed-grade L-valine. The values are not a regulatory monograph, but they reflect current industrial trade specifications and are verified using the listed reference methods. Because feed-grade L-valine is a free amino acid, extraction for chromatographic assay does not require acid hydrolysis; however, the assay value is expressed on a dry matter basis, so loss on drying must be determined before correcting the chromatographic result. The analytical uncertainty of HPLC methods is typically below 2% relative standard deviation when the sample matrix is limited to crystalline valine and its normal manufacturing impurities.

    ParameterTypical limit or rangeReference method
    AppearanceWhite to off-white crystalline powder or granulesVisual inspection
    Assay, L-valine, dry basis98.0–98.5%HPLC with post-column ninhydrin derivatization; ISO 13903:2005
    Loss on drying≤0.5%AOAC 930.15
    Residue on ignition≤0.1%USP 281
    Specific rotation [α]D25, c=5 in HCl+26.5° to +29.0°USP 781
    Lead, Pb≤5 mg/kgICP-MS after microwave digestion
    Arsenic, As≤1 mg/kgICP-MS after microwave digestion
    Heavy metals, as Pb≤10 mg/kgPharmacopoeial sulfide precipitation
    Bulk density0.50–0.70 g/cm³USP 616
    pH, 5% aqueous solution5.5–7.0USP 791

    At feed mill scale, feed-grade L-valine is received in 25 kg multi-wall paper bags with an inner polyethylene liner or in 500–1000 kg flexible intermediate bulk containers. The product is added through loss-in-weight screw feeders or vacuum conveying micro-dosing systems at rates of 0.10–3.50 kg/metric ton of complete feed, adjusted to the targeted standardized ileal digestible valine-to-lysine ratio. Batch-to-batch flow variability is influenced by moisture content and particle size distribution; when ambient relative humidity exceeds 60%, caking and bridging in hoppers and screw feeders can occur. In such conditions, the weigh hopper is purged with dry compressed air and the receiving mixer is re-validated with a microtracer salt to maintain a mixing coefficient of variation below 10%.

    The product is stable for 24 months from the date of manufacture when kept in unopened original packaging at or below 25 °C and 65% relative humidity. It is less hygroscopic than L-lysine monohydrochloride, but exposure to high-humidity air can induce surface dissolution and crystalline bridging. Because the product is supplied as a free amino acid, it does not contribute chloride or sodium to the final feed; blending with organic acids, phytase, or choline chloride requires no segregation beyond standard dry-mixing verification. Mixing with strongly alkaline mineral premixes is avoided to reduce the risk of Maillard-type reactions between amino groups and residual reducing sugars in some vegetable carrier materials.

    In compound feed plants, L-valine is most often incorporated into a micro-premix with limestone, rice hulls, or wheat bran as a carrier, then dosed into the main mixer. Segregation tests using a colored iron tracer or a riboflavin tracer are performed whenever a new carrier is introduced or when the addition point changes from the main mixer to a post-mixing pellet coating unit. If a post-pelleting liquid application is used, L-valine is not dispersible in oil and must be applied in a water-based suspension with a high-shear agitator; sedimentation in the spray line can occur if particle size exceeds 150 µm. Published data on liquid application of crystalline valine is limited compared with methionine or lysine. Thermal stability of L-valine during pellet conditioning is high relative to lysine or threonine; the melting point is near 315 °C with decomposition, and industrial pelleting at 80–85 °C conditioning temperature does not reduce assayable valine in finished pellets. Published data for specific extruder configurations at barrel temperatures above 120 °C is limited.

    When Valine Becomes the Next Limiting Amino Acid in Low-Crude-Protein Formulations

    In corn–soybean meal-based swine diets, the National Research Council (2012) requirement model reports a standardized ileal digestible valine-to-lysine ratio of 0.65 for growing pigs from 25 kg to 50 kg body weight, rising to approximately 0.85 for lactating sows. Practical commercial formulations often maintain a higher margin, typically 0.68–0.72 for grower pigs, to account for health challenge and feed intake variation. When soybean meal inclusion is reduced to lower total crude protein by 2–4 percentage points, intact feedstuffs no longer supply enough valine to meet these ratios, and feed-grade L-valine is used to correct the deficit. The supplementation response is most consistent when the total valine deficit is calculated from standardized ileal digestible valine values of the intact protein matrix rather than total valine.

    In broilers, published breeder nutrition specifications from Cobb 500 and Ross 308 indicate digestible valine-to-lysine ratios of 0.75–0.80 in starter phase diets and modestly lower ratios in finisher phases. Supplementation rates in complete feed generally fall between 0.3 kg and 1.2 kg per metric ton, depending on the intact protein matrix and the degree of crude protein reduction. The inclusion of feed-grade L-valine in such formulations permits a lower soybean meal concentration without increasing total nitrogen and ammonia excretion; published data on the resulting ammonia reduction is more consistent for pigs than for broilers. In nitrogen balance trials using swine metabolism cages, reductions in total nitrogen excretion of 8–15% have been reported when crude protein is lowered and supplemented with crystalline amino acids including valine; data for the specific valine contribution is limited.

    Incoming quality control at feed additive terminals commonly uses near-infrared reflectance spectroscopy with a pre-calibrated identity library for valine, plus wet-chemical confirmation of assay and specific rotation on retained samples from each delivery lot. Because bulk density and particle geometry affect near-infrared path length and dosing auger calibration, the calibration set must include material from the specific manufacturing site or model code. Failure to segregate reserved samples by production lot can invalidate traceability under feed hygiene regulation EC 183/2005. The product is not classified as dangerous goods under UN transport regulations and does not carry a hazard statement under Regulation (EC) No 1272/2008; it is stored away from strong oxidizers and open flames because organic amino acid dusts are combustible when dispersed in air.