Properties of Na2SO4 (Sodium sulfate):
Alternative NamesSodium sulphate Disodium sulfate Sulfate of sodium Thénardite (anhydrous mineral) Glauber's salt (decahydrate) ''Sal mirabilis'' (decahydrate) Mirabilite (decahydrate mineral) Elemental composition of Na2SO4
Related compounds
Sample reactions for Na2SO4
Sodium sulfate (Na2SO4): Chemical CompoundScientific Review Article | Chemistry Reference Series
AbstractSodium sulfate (Na2SO4) represents a fundamental inorganic salt with extensive industrial significance. This white crystalline solid exists in anhydrous form and multiple hydrated states, most notably the decahydrate (Na2SO4·10H2O), known historically as Glauber's salt. The compound demonstrates exceptional aqueous solubility characteristics, with solubility increasing dramatically from 4.76 grams per 100 milliliters at 0°C to a maximum of 49.7 grams per 100 milliliters at 32.384°C. Sodium sulfate serves as a crucial raw material in detergent manufacturing, pulp processing, glass production, and textile industries. With annual global production exceeding 6 million metric tons, it ranks among the most commercially significant inorganic compounds. The substance exhibits typical ionic behavior in solution and demonstrates remarkable thermal stability, with decomposition occurring only above 1000°C. IntroductionSodium sulfate stands as one of the most industrially important inorganic salts, serving as a fundamental chemical feedstock across multiple sectors. Classified unambiguously as an inorganic ionic compound, sodium sulfate consists of sodium cations (Na+) and sulfate anions (SO42-) in a 2:1 ratio. The compound's historical significance dates to 1625 when Johann Rudolf Glauber identified its decahydrate form in Austrian spring waters, designating it sal mirabilis (miraculous salt) due to its medicinal properties. Throughout the 18th and 19th centuries, sodium sulfate emerged as a critical intermediate in the Leblanc process for soda ash production, establishing its industrial relevance. Modern production methods yield approximately 6 million metric tons annually, with applications spanning from commodity chemicals to specialized industrial processes. Molecular Structure and BondingMolecular Geometry and Electronic StructureThe sulfate anion in sodium sulfate exhibits perfect tetrahedral symmetry (Td point group) with sulfur-oxygen bond lengths of 149 picometers. According to valence shell electron pair repulsion theory, the central sulfur atom adopts sp3 hybridization, resulting in ideal O-S-O bond angles of 109.5°. The electronic structure reveals formal charges of +2 on sulfur and -1 on each oxygen atom, with the sulfur atom employing its six valence electrons in bonding molecular orbitals. The sodium cations maintain octahedral coordination in crystalline forms, with Na-O distances measuring approximately 240 picometers in the decahydrate. Spectroscopic evidence from X-ray diffraction studies confirms the ionic character of Na-O bonds and predominantly covalent character within the sulfate polyatomic ion. Chemical Bonding and Intermolecular ForcesSodium sulfate demonstrates primarily ionic bonding characteristics between sodium cations and sulfate anions, with lattice energy estimated at -1947 kilojoules per mole. The sulfate ion itself contains highly polar covalent S-O bonds with bond dissociation energies of 523 kilojoules per mole. In the crystalline state, the decahydrate form exhibits extensive hydrogen bonding networks between water molecules and sulfate oxygen atoms, with O-H···O distances measuring 276 picometers. The compound's substantial dipole moment of 10.4 Debye reflects the significant charge separation within the sulfate ion. Van der Waals forces contribute minimally to the crystal cohesion energy, accounting for less than 5% of the total lattice energy. Comparative analysis with potassium sulfate reveals reduced ionic character in sodium sulfate due to the smaller cation size and higher charge density. Physical PropertiesPhase Behavior and Thermodynamic PropertiesAnhydrous sodium sulfate presents as a white crystalline solid with orthorhombic crystal structure and density of 2.664 grams per cubic centimeter. The compound melts at 884°C and boils at 1429°C under standard atmospheric pressure. The decahydrate form (Na2SO4·10H2O) undergoes phase transition at 32.384°C, melting with water release. Thermodynamic parameters include heat of fusion of 24.7 kilojoules per mole for anhydrous form and 78.2 kilojoules per mole for decahydrate. Specific heat capacity measures 128.2 joules per mole per kelvin at 298 K. The refractive index registers at 1.468 for anhydrous crystals and 1.394 for the decahydrate. Magnetic susceptibility measurements indicate diamagnetic behavior with χ = -52.0 × 10-6 cubic centimeters per mole. Spectroscopic CharacteristicsInfrared spectroscopy reveals characteristic sulfate vibrations: symmetric stretch at 981 cm-1, asymmetric stretch at 1104 cm-1, and bending modes at 451 cm-1 and 617 cm-1. Raman spectroscopy shows strong polarization at 992 cm-1 corresponding to the totally symmetric stretching mode. Nuclear magnetic resonance spectroscopy demonstrates a singlet at 67.6 ppm for 33S in dimethyl sulfoxide solution. UV-Vis spectroscopy indicates no absorption in the visible region, consistent with its white appearance, with charge-transfer transitions occurring below 200 nanometers. Mass spectrometric analysis of vaporized samples shows predominant fragments at m/z = 142 (Na2SO4+), 102 (NaSO4+), and 80 (SO3+). Chemical Properties and ReactivityReaction Mechanisms and KineticsSodium sulfate demonstrates typical ionic sulfate reactivity, serving as a sulfate ion source in precipitation reactions. The compound shows remarkable thermal stability, decomposing only above 1000°C to sodium oxide and sulfur trioxide. Carbothermal reduction proceeds at 800°C with activation energy of 158 kilojoules per mole, yielding sodium sulfide and carbon dioxide. Reaction with concentrated sulfuric acid produces sodium bisulfate with second-order kinetics and rate constant of 3.4 × 10-4 liters per mole per second at 25°C. Double salt formation with other alkali metal sulfates occurs readily, with 3Na2SO4·K2SO4 (aphthitalite) crystallizing in hexagonal system. The compound remains inert toward most oxidizing and reducing agents under standard conditions. Acid-Base and Redox PropertiesThe sulfate anion represents the conjugate base of bisulfate ion, with pKa2 of 1.99 for sulfuric acid dissociation. Sodium sulfate solutions exhibit neutral pH (6.5-7.5) due to the negligible hydrolysis of sulfate ion. Redox properties indicate stability in both oxidizing and reducing environments, with standard reduction potential E° = -0.36 V for the SO42-/SO32- couple. Electrochemical measurements show no significant oxidation or reduction waves within the water stability window. The compound demonstrates exceptional stability across pH ranges from 2 to 12, with decomposition occurring only under extreme acidic or basic conditions at elevated temperatures. Synthesis and Preparation MethodsLaboratory Synthesis RoutesLaboratory preparation typically employs neutralization of sodium hydroxide with sulfuric acid: 2NaOH(aq) + H2SO4(aq) → Na2SO4(aq) + 2H2O(l). This highly exothermic reaction (ΔH = -112.5 kilojoules per mole) proceeds quantitatively at room temperature. Alternative routes include the reaction of sodium bicarbonate with magnesium sulfate: 2NaHCO3 + MgSO4 → Na2SO4 + MgCO3 + CO2 + H2O. Purification involves recrystallization from water below 32°C to obtain the decahydrate, followed by careful dehydration at 100°C to produce anhydrous material. The product typically achieves 99.5% purity with major impurities including calcium, magnesium, and iron sulfates. Industrial Production MethodsIndustrial production derives from both natural and synthetic sources, with approximately two-thirds obtained from mineral deposits. The Mannheim process represents the primary chemical route: 2NaCl + H2SO4 → 2HCl + Na2SO4, operated at 500-600°C in muffle furnaces. The Hargreaves process offers an alternative: 4NaCl + 2SO2 + O2 + 2H2O → 4HCl + 2Na2SO4, utilizing sulfur dioxide from pyrite roasting. Natural production involves mining of mirabilite (Na2SO4·10H2O) deposits from alkaline lakes, with major operations in Canada, Spain, and China. Economic factors favor natural production where geographically feasible, with production costs ranging from $30-$130 per metric ton depending on purity. Analytical Methods and CharacterizationIdentification and QuantificationQualitative identification employs precipitation with barium chloride, forming insoluble barium sulfate with detection limit of 10 micrograms per milliliter. Quantitative analysis utilizes gravimetric methods via barium sulfate precipitation, achieving accuracy of ±0.5% and precision of ±0.2%. Ion chromatography provides rapid determination with separation on anion-exchange columns and conductivity detection, achieving detection limits of 0.1 micrograms per milliliter. Atomic absorption spectroscopy measures sodium content after appropriate dilution, while inductively coupled plasma optical emission spectrometry enables simultaneous determination of sodium and sulfate sulfur. X-ray diffraction analysis confirms crystalline structure and polymorph identity through comparison with reference patterns. Purity Assessment and Quality ControlIndustrial specifications typically require minimum 99.0% Na2SO4 content with maximum limits of 0.5% water, 0.05% chloride, 0.05% iron, and 0.005% heavy metals. Pharmacopeial standards for medicinal grades specify tighter constraints, including pH range 6.0-8.0 and limits on arsenic (3 ppm) and lead (10 ppm). Stability testing indicates indefinite shelf life under dry conditions, though the decahydrate form effloresces at relative humidities below 65%. Thermal analysis methods including differential scanning calorimetry and thermogravimetric analysis monitor dehydration behavior and phase transitions. Particle size distribution analysis ensures consistency for industrial applications, particularly in detergent formulations. Applications and UsesIndustrial and Commercial ApplicationsDetergent manufacturing consumes approximately 50% of global production, where sodium sulfate serves as processing aid and filler in powdered formulations. The pulp industry employs sodium sulfate in the Kraft process as makeup chemical for sulfur losses, though consumption has declined from 1.4 million tons annually in 1970 to approximately 150,000 tons currently. Glass production utilizes 110,000 tons annually as fining agent to remove air bubbles from molten glass, with optimal concentration of 0.5-1.5% by weight. Textile dyeing applications exploit its electrolyte properties for leveling dyes, with Japanese industry consuming 100,000 tons annually. The compound serves as freezing-point depressant in refrigerated transportation and as inert filler in various industrial products. Research Applications and Emerging UsesMaterials science research investigates sodium sulfate decahydrate as phase change material for thermal energy storage, with heat of fusion of 252 kilojoules per kilogram. Solar heating systems incorporate the compound for passive heat storage due to its favorable phase transition temperature of 32°C. Electrochemical studies employ sodium sulfate as supporting electrolyte in various systems due to its electrochemical inertness. Emerging applications include use as crystal habit modifier in industrial crystallization processes and as porogen agent in ceramic manufacturing. Patent activity focuses on improved purification methods and composite materials incorporating sodium sulfate for thermal management. Historical Development and DiscoveryJohann Rudolf Glauber's 1625 discovery of sodium sulfate decahydrate in Austrian spring waters marked the compound's introduction to Western science. His treatise Descriptio Novi Phosphori (1651) detailed the preparation and medicinal properties of sal mirabilis, establishing its use as a purgative. Eighteenth-century applications expanded to industrial scale when sodium sulfate became crucial for soda ash production via the Leblanc process, patented in 1791. The nineteenth century witnessed massive scale-up of production, particularly in England where chemical factories produced sodium sulfate as key intermediate. Twentieth-century developments included the shift from synthetic to natural sources and the decline of traditional applications with the rise of alternative technologies. Modern production maintains stable output despite changing application patterns. ConclusionSodium sulfate remains a compound of substantial industrial and scientific importance despite its simple chemical formula. Its unique solubility characteristics, thermal stability, and ionic nature facilitate diverse applications across multiple sectors. The compound's historical significance in chemical industry development underscores its fundamental role in inorganic chemistry. Future research directions include optimization of production methods from alternative sources, development of advanced applications in energy storage, and refinement of analytical techniques for quality control. The continued economic viability of sodium sulfate production ensures its persistence as a key industrial chemical in the foreseeable future. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
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The database includes melting points, boiling points, densities, and alternative names collected from various chemical sources. What are compound properties?Chemical compound properties include physical characteristics such as melting point, boiling point, and density, which are important for chemical identification and applications. Alternative names help identify the same compound when referenced by different naming conventions.How to use this tool?Enter a chemical formula (like H2O) or compound name (like water) to look up available properties and alternative names. The tool will search through the database and display any available physical properties and known alternative names for the compound. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
