| HS Code | 208571 |
| Product Name | Sodium Selenite Anhydrous ≥99% |
| Chemical Formula | Na2SeO3 |
| Molecular Weight | 172.94 g/mol |
| Cas Number | 10102-18-8 |
| Ec Number | 233-267-9 |
| Mdl Number | MFCD00003468 |
| Purity | ≥99% |
| Appearance | White to off-white crystalline powder |
| Density | 3.1 g/cm3 |
| Melting Point | 350 °C (decomposes) |
| Solubility In Water | 85 g/100 mL at 20 °C |
| Storage Conditions | Keep in a cool, dry, well-sealed container |
| Hazard Classification | Toxic if swallowed or inhaled; dangerous to the environment |
As an accredited Sodium Selenite Anhydrous ≥99% factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg fiber drums with double polyethylene liners, sealed tightly and labeled for safe handling and storage. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Sodium Selenite Anhydrous ≥99% packed in drums, palletized, and securely stowed for safe transport. |
| Shipping | Sodium Selenite Anhydrous ≥99% ships as UN 2630 Selenites, Hazard Class 6.1, Packing Group I. It is a highly toxic solid requiring UN-approved packaging, a toxic substance label, and complete shipping documentation. Keep segregated from food and acids, and ensure transporter is authorized to handle dangerous goods. |
| Storage | Store Sodium Selenite Anhydrous (≥99%) in a tightly sealed container in a cool, dry, well-ventilated area. Protect from moisture and humidity, as it is hygroscopic. Keep away from acids, reducing agents, and incompatible materials. Label clearly, use secondary containment, and store separately from foodstuffs and personal items. |
| Shelf Life | Shelf life is typically 2-3 years if stored tightly sealed in a cool, dry place away from light and moisture. |
In container-glass manufacturing, the redox state of the silicate melt directly controls the equilibrium between Fe(II) and Fe(III), and green iron absorption is not corrected by removing iron alone but by imposing a selenium-based oxidation–reduction compensation that shifts the transmission spectrum toward the neutral grey region. Sodium selenite anhydrous at ≥99% purity is introduced into the batch house as a micro-ingredient because its 45.6 wt% selenium content allows direct replacement calculations against elemental selenium and sodium selenate. Commercial batch loading data for flint container and float glass lines indicate sodium selenite additions in the range 0.001–0.007 wt% of dry batch, equivalent to 0.0005–0.003 wt% selenium. The relevant finished-product compliance anchors are ASTM C1036-21 for flat glass optical quality and EN 572-1:2012 for basic soda-lime silicate glass; these standards do not prescribe selenium dosage, but the optical uniformity classes and point-defect limits in ASTM C1036-21 constrain the permissible color compensation because residual pink or grey transmittance becomes a grading defect above 0.01 wt% selenium input.
The manufacturing sequence for selenium decolorization is controlled at the weigh-belt and melter charge stages rather than by post-melting adjustment. A dedicated micro-ingredient dosing unit with a tolerance of ±0.5% is required because normal aggregate scale resolution cannot discriminate selenium loadings in the region of 1–7 kg per 100 t of batch. The dry charge then passes through a tumble mixer before doghouse charging, and melting proceeds at 1,450–1,550 °C in regenerative or oxy-fuel furnaces. Selenium volatilizes in the early melt zone, and retention is strongly reduced when high cullet ratios introduce carbonaceous residues; production experience indicates that selenium retention can fall below 40% of the added amount under reducing packages, while oxidizing packages using sodium nitrate at 0.5–2.0 kg/t batch preserve a higher retained fraction. Baghouse and electrostatic precipitator systems on the furnace exhaust are monitored by EPA Method 29 for total selenium because volatile selenite decomposition products must be controlled before stack discharge. The terminal product from this application is clear flint container glass for pharmaceutical and beverage packaging, and low-iron float glass for architectural glazing; in both cases the internal release specification is commonly tied to a maximum discrete wavelength shift in the 500–560 nm transmission band measured according to ASTM E308.
Selenium premix homogeneity in production-scale feed mills is governed less by total selenium content than by the particle-size distribution of the sodium selenite carrier and the sequence of micro-ingredient addition. Sodium selenite anhydrous at ≥99% purity is used as the water-soluble inorganic selenium source because it converts to bioavailable selenite in the gastrointestinal tract and is included in complete feed at legally constrained rates. The compliance framework is anchored by 21 CFR 573.920 in the United States, which permits selenium supplementation in animal feed only through specific forms and within maximum dietary concentrations, and by Regulation (EC) No 1831/2003 in the European Union, under which sodium selenite is classified as a nutritional feed additive for all animal species. For a 1% inclusion mineral premix, the sodium selenite anhydrous addition is typically 0.02–0.06 g/kg premix, which delivers 0.09–0.27 mg Se/kg complete feed when the premix is diluted at 1:99 into the final ration.
The process route in a dedicated premix plant commences with pre-grinding of sodium selenite anhydrous to a D50 below 50 µm, followed by dry blending with calcium carbonate or ground rice hulls to create a 0.1–1% selenium working premix that can be handled with standard micro-dosers. The working premix is discharged into a horizontal ribbon mixer with an effective volume of 1,000–2,000 L; batch-to-batch coefficient of variation for selenium is checked by sampling according to ISO 6497 and is maintained below 5% for pelleted feed, while mash feed lines with poor carrier affinity may show segregation if the mixer is filled above 70% of working volume. Sodium selenite is incompatible with reducing agents in the same premix, including ascorbic acid and certain aldehydic feed preservatives, because partial reduction to elemental selenium produces grey specks and lowers measured soluble selenium. The terminal products are complete pelleted feeds for poultry and swine, 0.5–5% mineral premixes, and selenium-fortified salt blocks; in each case the label claim is verified by ICP-MS after nitric acid digestion per EN 17053:2018 or equivalent AOAC methods.
The function of selenite in the catholyte of electrolytic manganese metal cells is not that of a bulk reagent but of a selective deposition regulator on the titanium cathode surface. In cells operating at 35–45 °C with cathodic current density of 300–400 A/m², the selenite ion discharges near the manganese nucleation site and modifies the overpotential for metal deposition, reducing hydrogen evolution and raising current efficiency. The working electrolyte concentration of sodium selenite is maintained between 0.07–0.11 g/L, equivalent to 0.03–0.05 g/L selenium, in a sulfate electrolyte containing 35–40 g/L Mn²⁺ and 100–120 g/L ammonium sulfate at pH 6.5–7.2. Process control requires ion chromatography or voltammetric monitoring of selenite because excess addition above 0.11 g/L leads to selenium co-deposition and brittle cathode edges, while deficiency below 0.07 g/L reduces current efficiency and increases anodic sludge formation.
During continuous production, the purified leach solution is fed through flow distributors to the cathode compartments, and spent electrolyte is recycled after anolyte purification. The terminal product is electrolytic manganese metal flake with Mn ≥99.7%, supplied to steel desulfurization, aluminum alloying, and welding electrode coating operations. Effluent control for this application is governed by GB 8978-1996, under which total selenium in discharge to Class I receiving waters must be below 0.1 mg/L; workplace exposure to selenium compounds is further controlled under ACGIH TLV-TWA at 0.2 mg/m³ as selenium.
When cadmium sulfoselenide pigments are calcined under a reducing or inert atmosphere, sodium selenite anhydrous provides the Se(IV) intermediate that is reduced to cadmium selenide within the CdS lattice, shifting the band gap from yellow to red-orange. In zircon-encapsulated ceramic pigment syntheses, the calculated sodium selenite loading corresponds to 5–20 wt% selenium in the pigment precursor blend, depending on whether the target hue is orange, red, or maroon; exact loading data for proprietary encapsulant matrices are limited, and the required addition is normally derived from the molar Cd:Se ratio rather than from a fixed pigment-weight percentage. The production process involves high-shear wet milling of cadmium carbonate or cadmium oxide with sulfur and sodium selenite, followed by calcination at 950–1,150 °C in a sealed rotary kiln with oxygen exclusion, then acid washing and jet milling to an agglomerate-free D50 below 5 µm for ceramic inkjet application. The compliance boundary is Directive 84/500/EEC for cadmium release from ceramic glazes intended for food contact, supplemented by ISO 6486-1 for global trade testing; cadmium sulfoselenide pigments are restricted from plastic and toy applications under REACH Annex XVII entry 23. Terminal product types include ceramic in-glaze red pigments for porcelain tableware, sanitaryware, and architectural ceramic tile inks.
Aqueous electrodeposition routes to CuInSe₂ and Cu(In,Ga)Se₂ absorber films use sodium selenite anhydrous as the Se(IV) source because selenite is soluble in acidic sulfate baths and can be codeposited with Cu(I) and In(III) at moderate cathodic potentials. Published bath formulations for laboratory-scale CIGS deposition use sodium selenite at 5–15 mmol/L, copper sulfate at 10–20 mmol/L, and indium sulfate at 20–30 mmol/L, with pH held between 1.8–2.5 and bath temperature at 25–40 °C. Deposition is performed potentiostatically at −0.6 to −0.8 V vs SCE on molybdenum-coated soda-lime glass or flexible stainless steel substrates. The as-deposited precursor film is then annealed at 450–550 °C under selenium or argon to form the chalcopyrite phase; failure to control selenite reduction current produces metallic selenium inclusions and secondary Cu₂Se phases. The terminal products are CIGS thin-film photovoltaic modules evaluated under IEC 60904-3:2019 for current-voltage characteristics, and flexible photovoltaic laminates for building-integrated photovoltaics.
Scale-up from Hull cell to roll-to-roll plating requires insoluble iridium oxide anodes and electrolyte recirculation because selenite can be cathodically stripped unevenly across wide-web substrates. Bath analysis after each 50 Ah/L of charge throughput is recommended to prevent drift in Se:Cu ratio and the resulting shift in absorber composition from CuIn₀.₇Ga₀.₃Se₂ stoichiometry.
Commercially, selenium-enriched yeast fermentation uses sodium selenite anhydrous as the water-soluble inorganic selenium source because it can be sterilized, dosed incrementally, and taken up by Saccharomyces cerevisiae during the exponential growth phase. In stirred-tank bioreactors of 10–50 m³, the sodium selenite feed solution is added at rates that maintain residual selenite in the supernatant below 5 mg/L, with total batch selenium input typically in the range 20–50 mg/L culture medium, because higher residual concentrations inhibit yeast growth and reduce incorporation into selenomethionine. The process is operated as a fed-batch fermentation at 28–30 °C, pH 5.0–5.5, and dissolved oxygen above 20% saturation, followed by centrifugal harvest, pasteurization, spray drying, and final particle-size reduction to pass a 100 mesh screen. Compliance for the resulting inactivated selenized yeast in feed is under Regulation (EC) No 1831/2003 and 21 CFR 573.920; industrial sodium selenite anhydrous must be evaluated for sulfate and chloride residues before fermentation because those impurities alter yeast membrane transport kinetics. The terminal product is an organic selenium yeast powder for poultry and dairy premixes, providing selenomethionine as the dominant selenium species instead of the inorganic selenite input.
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Commercial availability of sodium selenite anhydrous ≥99% is defined by a compact set of identity parameters rather than by a single marketing designation. The material is the disodium salt of selenious acid, CAS 10102-18-8, EC 233-267-9, molecular formula Na₂SeO₃, molar mass 172.94 g/mol, and selenium content 45.65 wt% on the anhydrous basis. It appears as a white to off-white crystalline powder or granular solid, depending on spray-drying or crystallizer conditions in the manufacturer’s isolation step. Unlike the pentahydrate, the anhydrous material has no lattice water to compensate for ambient humidity; therefore the loss on drying specification is typically ≤0.5% by gravimetric method at 105 °C to constant weight. Producers generally synthesize the compound by dissolving selenium dioxide in aqueous sodium hydroxide and driving the reaction to the selenite oxidation state, followed by concentration, crystallization, and drying under low-humidity air or nitrogen. The ≥99% assay is determined by iodometric titration or inductively coupled plasma optical emission spectroscopy against a reference standard, with the assay reported on the dried basis. This product is used where water introduction, caking, or storage instability from the hydrated form is unacceptable, such as dry-glass batch systems, trace-element feed premixes, and non-aqueous reagent preparations.
Three related selenium salts are frequently confused in purchasing specifications. Sodium selenite anhydrous, Na₂SeO₃, contains 45.65 wt% selenium; sodium selenite pentahydrate, Na₂SeO₃·5H₂O, contains approximately 30.0 wt% selenium because the five water molecules dilute the active ion. The anhydrous form is selected when downstream processing requires a low water content or when the feed premix or glass batch is formulated on a selenium-equivalent basis and carrier moisture would interfere with analytical verification. Sodium selenate, Na₂SeO₄, is the +6 oxidation state and has a selenium content of 41.79 wt%; its redox behavior is materially different, because selenate is more stable under alkaline oxidizing conditions and is reduced more slowly to bioavailable selenide in biological systems. In glass melting, selenite can act as a redox fining or decolorizing agent through its reduction to elemental selenium and then volatilization, whereas selenate can require higher temperature or a stronger reducing furnace environment to produce the same selenium vapor contribution. In animal nutrition, 21 CFR 573.920 permits sodium selenite and sodium selenate as sources of selenium in feed, but the two salts are not freely interchangeable at equal selenium equivalents without reformulation and regulatory verification.
| Property | Sodium Selenite Anhydrous | Sodium Selenite Pentahydrate | Sodium Selenate |
|---|---|---|---|
| Selenium content | 45.65 wt% | 30.02 wt% | 41.79 wt% |
| Selenium oxidation state | +4 | +4 | +6 |
| Water of crystallization | None | 5 mol H₂O | None |
| Typical function | Low-moisture glass decolorizing, dry feed premix dilution, non-aqueous reagent synthesis | Aqueous stock solutions, feed applications where water is not critical | Higher-oxidation selenium source, analytical reference, selenium biofortification |
| Key handling difference | Hygroscopic; requires sealed dry storage | Can lose water or cake above 30 °C | Stronger oxidizing potential; reductive incompatibilities differ |
A representative certificate of analysis for the ≥99% product includes more than the total selenium assay. Purchasing specifications often define selenate, chloride, sulfate, iron, lead, cadmium, mercury, arsenic, and loss on drying. The selenate limit matters for glass redox calculations, because selenate carries an additional oxygen atom and changes the batch oxidation state; in feed premixes, the heavy metal limits align with regional feed additive regulations. The term ≥99% refers to total sodium selenite anhydrous content, not elemental selenium content. Limits are often reported on an as-is basis unless marked “dried basis”; in low-moisture warehousing, the difference between as-is and dried basis is below 0.2%. Because selenite can oxidize to selenate under prolonged exposure to warm air, the selenate content is monitored as a stability indicator, not only a purity parameter.
| Parameter | Limit | Analytical basis |
|---|---|---|
| Assay Na₂SeO₃ | ≥99.0% | Iodometric titration or ICP-OES |
| Loss on drying | ≤0.5% | Gravimetric, 105 °C |
| Selenate, SeO₄ | ≤0.3% | Ion chromatography |
| Chloride, Cl | ≤0.05% | Turbidimetric or titration |
| Sulfate, SO₄ | ≤0.05% | Turbidimetric |
| Iron, Fe | ≤0.001% | ICP-OES after dissolution |
| Heavy metals as Pb | ≤0.001% | USP <231> or AAS |
| Arsenic, As | ≤0.0003% | Hydride-generation AAS |
| Cadmium, Cd | ≤0.0001% | ICP-MS |
| Mercury, Hg | ≤0.0001% | Cold-vapour AAS |
European feed additive enforcement commonly relies on inductively coupled plasma mass spectrometry after microwave digestion, with EN 17053:2018 cited for trace element determination in animal feeding stuffs. Sampling should use a clean stainless steel thief or core sampler inserted through the full bed depth; sample splitting via rotary riffle prevents particle-size segregation. ISO 9001:2015 certification is a minimum supplier quality requirement, but it does not replace lot-specific selenium speciation when the product is used for oxidation-sensitive applications.
Container glass and float glass producers use selenium compounds to offset the green tint from iron impurities. Selenium in the +4 oxidation state can be reduced in the batch or glass melt to elemental selenium, which produces a pink to red complementary color that neutralizes the ferrous iron blue-green absorption. Sodium selenite anhydrous is preferred when the batch contains recycled cullet and reducing agents such as anthracite or slag, because its low water content avoids hydrolysis reactions that can generate steam pockets or contribute to batch carry-over. The exact addition rate is not a fixed constant; it depends on the iron redox ratio, total iron content, furnace atmosphere, melt temperature, and cullet quality. Iron in container glass is commonly 0.02–0.5 wt% Fe₂O₃, and finished-glass selenium concentrations are typically controlled below 150 ppm to avoid grey or brown bronzing. Published batch sheets have described selenium additions corresponding to 0.005–0.05 wt% of selenium in batch, but published data for this specific configuration is limited and actual use must be optimized by laboratory melts. In oxy-fuel furnaces, selenium retention may be higher than in regenerative furnaces; producers typically measure the selenium volatilization loss by X-ray fluorescence on glass samples and adjust the premix feed rate.
A sodium selenite anhydrous premix is often dispersed in soda ash or silica sand before addition to avoid localized high selenium concentrations that cause cord or color streaks. The anhydrous product’s low moisture specification is advantageous in dry batch handling systems using screw feeders and pneumatic conveying, where moisture above 0.5% could cause bridging in hoppers or build-up on conveyor flights. The product is not a direct substitute for selenium metal or selenium dioxide on a kilogram-for-kilogram basis. Selenium metal provides higher selenium concentration but requires more aggressive oxidation before it participates in color compensation; selenium dioxide is volatile and corrosive, complicating handling. Sodium selenite anhydrous offers a nonvolatile salt matrix that can be dry-blended and weighed without dedicated fume extraction beyond standard particulate controls, although selenium compounds remain toxic and require engineering controls. Furnace emissions are controlled through baghouse or electrostatic precipitator capture of selenium oxide particulates, and wet scrubber blowdown must be treated because selenium is regulated in wastewater discharge permits.
Sodium selenite anhydrous is used as a selenium source in animal feed at trace levels. Under 21 CFR 573.920, selenium from sodium selenite may be added to a complete feed at 0.3 mg/kg for chickens, turkeys, swine, cattle, and sheep, but this is a regulatory maximum rather than a formulation target; typical supplemental rates are lower and must account for background selenium in grain and oilseed meal. The anhydrous grade is integrated into a microingredient premix through a two-stage dilution. A concentrated premix at 0.5–2.0% selenium is prepared in a ribbon mixer or paddle mixer with a coefficient of variation below 5% for selenium by EN 17053:2018 or ICP-MS after microwave digestion. Because the final complete feed inclusion rate is on the order of 0.01–0.05 kg per tonne of diluted premix, direct addition of the pure salt to a mixer is not acceptable due to poor distribution and risk of selenium toxicosis in localized feed pockets. The anhydrous powder is often milled or conditioned to pass a 60-mesh screen to improve dispersibility. Low moisture is critical when the premix includes choline chloride or other hygroscopic components, because free water can initiate caking and accelerate vitamin oxidation.
Trace mineral premixes containing copper, zinc, and manganese sulfates can create acidic microenvironments. Sodium selenite is compatible in dry blends but should not be pre-dissolved with reducing sugars or ascorbic acid at low pH, because selenite can be reduced to elemental selenium, producing a red precipitate that is poorly bioavailable. Formulators therefore segregate the selenium source from reducing agents in the premix or use a coated product. Published batch records from feed mills indicate that mixing time must be validated; common double-ribbon mixers with a working volume of 2,000 kg require 12–20 min to reach acceptable selenium distribution when the selenium is added as a 1% premix. This is a process-specific parameter and must be verified by sampling at multiple mixer locations. In nutritional terms, sodium selenite is an inorganic source that enters the selenide pool for selenoprotein synthesis, whereas selenomethionine is incorporated into methionine-containing proteins. This difference influences tissue selenium deposition but does not make one source universally superior; the choice is driven by regulatory, formulation, and cost constraints.
Reagent-grade sodium selenite anhydrous serves a narrower but analytically demanding role in selenization reactions and nanoparticle synthesis. In laboratory-scale synthesis, the anhydrous form is preferred over the pentahydrate when the reaction solvent is non-aqueous or when stoichiometric calculations require exact selenium content. Residual water above 0.5% can quench moisture-sensitive intermediates or shift the concentration of selenium precursor solutions. When a 1,000 mg/L selenium stock solution is prepared gravimetrically, the anhydrous salt yields 456.5 mg selenium per gram of compound; a formulation error greater than 1% can occur if pentahydrate is mistaken for anhydrous. In the preparation of selenium nanoparticles via reduction with ascorbic acid or glutathione, the initial selenite concentration is typically 1–10 mmol/L, and the anhydrous product allows direct gravimetric preparation without correcting for lattice water. For example, a selenium concentration of 2.5 mmol/L can be prepared by dissolving 0.432 g of anhydrous sodium selenite per litre. The reduction proceeds rapidly at pH 4–6, producing elemental selenium; at higher pH the reaction rate decreases.
The material should not be combined with strong reducing agents or concentrated acids before the intended reaction, because selenite is reduced to elemental selenium or selenious acid, which may release toxic selenium dioxide vapor at elevated temperature. Safety data sheets require local exhaust ventilation and nitrile gloves; the ACGIH TLV for selenium and inorganic compounds as Se is 0.2 mg/m³ inhalable fraction. Storage in sealed glass or HDPE containers under argon or nitrogen is required after opening; ambient carbon dioxide does not react significantly, but humidity above 40% RH can cause water uptake and caking. The shelf life in tightly closed containers is often specified as 24 months by suppliers. All waste streams containing selenium must be treated as hazardous under local regulations; the material is toxic to aquatic life and is not to be released to drain.