Sodium

    group 1 · period 3 · s-block · alkali metal

    fullSodium is the conservative cation of water: the major ion of seawater and brackish water, an EU indicator parameter at 200 mg/L, a taste and dietary concern rather than a toxicant, the ion that softeners and every sodium reagent (hypochlorite, caustic, soda ash, bicarbonate, brine) add to water, and, as the sodium adsorption ratio, the number that decides whether an irrigation water ruins the soil.

    Typical wastewaters

    • municipal sewage Na⁺, conservative; sewage effluent carries the sodium of treatment chemicals (fluoride, bicarbonate, hypochlorite up to 30 mg/L together) and of domestic softeners (over 300 mg/L)
    • textile wet processing Na⁺ with chloride and sulfate from dyeing salt and neutralisation, reported as total dissolved solids; not removed by a standard effluent plant
    • desalination brine (reverse osmosis concentrate, thermal distillation) Na⁺ with Cl⁻ concentrated from seawater or brackish water; the marine discharge specification exempts desalination brine
    • ion exchange regenerant (softener spent brine) NaCl brine carrying the exchanged calcium and magnesium; spent brine disposal is the environmental cost of ion exchange
    • road de-icing runoff NaCl salt runoff to surface water and groundwater
    In the ledger's plant and process records, discharged by: Cleaning-in-place and disinfection (Food and beverage) · Cleaning (Food and beverage) · Meat processing (Food and beverage) · Thawing processes (Food and beverage) · Cyanides (sodium and potassium cyanide) (Chemicals) · Toluene diisocyanate and methylene diphenyl diisocyanate (Chemicals) · Canning (Food and beverage) · Cheese (Food and beverage) · Deheading and gutting (Food and beverage) · Drying (Food and beverage) · Filleting and skinning (Food and beverage) · Fish and shellfish processing (Food and beverage) · Freezing/Thawing (Food and beverage) · Grading (Food and beverage) · Salting (Food and beverage) · Scaling (Food and beverage) · Smoking (Food and beverage) · Thawing by 100 % water-saturated heated air (Food and beverage) · Thawing by sprinkling (Food and beverage) · Thawing in containers filled with warm water with air bubbles at the bottom (Food and beverage) · Thawing using water recirculation and air stirring (Food and beverage) · Gold leaching with cyanide (Mining) · Leaching (Mining)

    1 · Identity

    Symbol, number
    Na, 11
    Oxidation states in water
    +1 only, as the hydrated Na⁺ ion; no hydrolysis, no complexes of consequence, no insoluble salts in fresh water (the element entry: almost every sodium salt is soluble). Sodium is what is left when everything else has been removed, which is why it leaves treatment plants as salinity.
    Note
    The element entry carries the metal, halite, soda ash and caustic soda production. This chapter is sodium as a dissolved ion, as a reagent counter-ion and as sodicity. Sodium hypochlorite chemistry is in the chlorine chapter, the carbonate equilibria in the carbon chapter, and the dechlorination sulfite salts in the chlorine chapter.

    2 · Occurrence in water

    Natural sources
    Sodium is ubiquitous in water because its salts are so soluble; it is leached from the terrestrial environment to groundwater and surface water, and seawater is the reservoir (WHO background document). Saline intrusion, mineral deposits and sea spray raise it; sodium bicarbonate groundwater forms where calcium is exchanged for sodium on clays, giving soft, high sodium, high fluoride and high boron water (general geochemistry).
    Anthropogenic sources
    Sewage effluent, road de-icing salt, and treatment chemicals: sodium fluoride, sodium bicarbonate and sodium hypochlorite together can add up to 30 mg/L and domestic water softeners over 300 mg/L (WHO); industrial brines, reverse osmosis concentrate, ion exchange regenerant, caustic soda and soda ash dosing, and the sodium salts of every industry (textile dyeing salt, chlor-alkali, pulp, food).
    matrixtypical rangenote
    drinking water, typicalbelow 20 mg/Lregion-dependent; old surveysmost supplies; can exceed 250 mg/L in some countries; a 1963 to 1966 US survey of 2100 samples ranged 0.4 to 1900 mg/L with 42 percent above 20 mg/L and 5 percent above 250 mg/L; a later survey of 630 systems ranged below 1 to 402 mg/L
    groundwater supplies, US (989 community systems)median 16.4; 99th percentile 517 mg/LUS survey37 percent above 30 mg/L and 13 percent above 120 mg/L in the National Inorganic and Radionuclide Survey
    surface water, US rivers20 (Mississippi) to 120,000 (Great Salt Lake) mg/Lextremes, not a distributionthe range the EPA advisory quotes for US surface waters
    seawater10,800 mg/Lsingle figureoceanic abundance figure, Jefferson Lab via PubChem, quoted in the element entry
    drinking water after domestic softeningover 300 mg/Lcan reach this; usually much lower; the stoichiometry adds 0.46 mg sodium per mg of hardness as CaCO₃ exchanged
    municipal and industrial wastewaternot read no effluent survey read; textile effluent salt is high enough that ZDHC requires TDS to be reported ahead of a future limit

    3 · Speciation

    Sodium is Na⁺ everywhere in water: no hydrolysis, no redox, no precipitation, ion pairs with sulfate and carbonate that matter only in brines. It is conservative, so it tracks salinity, and its ratio to calcium and magnesium (the sodium adsorption ratio, SAR) rather than its concentration decides its effect on soil: a high sodium, low calcium water disperses clay and destroys infiltration (FAO 29). Its taste threshold depends on the anion: about 20 mg/L as sodium carbonate, 150 as chloride, 190 as nitrate, 220 as sulfate and 420 as bicarbonate at room temperature (WHO).

    conditiondominant speciesnote
    all natural and treated waterNa⁺ (hydrated)conservative; passes every process except membranes, distillation and ion exchange
    irrigation water with a high ratio of sodium to calcium plus magnesiumNa⁺ exchanging onto soil clay for Ca²⁺ and Mg²⁺sodic soil, reduced infiltration; evaluate SAR together with electrical conductivity (FAO 29)
    brines and reverse osmosis concentrateNa⁺ with NaSO₄⁻ and NaCO₃⁻ ion pairsnot relevant below a few g/L
    Solubility
    Sodium chloride 357 g/L and sodium carbonate 71 g/L at 0 C (WHO); all common sodium salts dissolve freely, so sodium has no solubility control in water and is never removed by precipitation.
    Hydrolysis
    None; Na⁺ is neither an acid nor a base in water. The pH of a sodium salt solution is that of its anion (carbonate alkaline, chloride neutral).
    Complexation
    Negligible; weak outer sphere ion pairs with sulfate and carbonate only at high ionic strength (general; not quantified in the sources read).
    Precipitates
    None from water. Sodium is the counter-ion left in solution when calcium, magnesium and metals are precipitated with sodium reagents.
    2RNa+CaX2+RX2Ca+2NaX+\ce{2 RNa + Ca^2+ -> R2Ca + 2 Na^+}
    cation exchange softening on a strong acid resin in the sodium form (R is the resin site); the same for Mg^2+; every equivalent of hardness removed adds one equivalent of sodium, 0.46 mg Na per mg CaCO3 (MWH chapter 16)
    RX2Ca+2NaCl2RNa+CaClX2\ce{R2Ca + 2 NaCl -> 2 RNa + CaCl2}
    regeneration with brine at 80 to 320 g NaCl per litre of resin (MWH chapter 16, from the chapter); the spent brine carries the hardness plus the excess salt
    NaOHNaX++OHX\ce{NaOH -> Na^+ + OH-}
    caustic soda dosing for pH elevation and metal hydroxide precipitation; adds 0.58 mg sodium per mg NaOH by the atomic weights and no hardness, the reason it replaces lime where sludge or scaling matter
    NaX2COX3+CaX2+CaCOX3(s)+2NaX+\ce{Na2CO3 + Ca^2+ -> CaCO3 (s) + 2 Na^+}
    soda ash removal of non-carbonate hardness after lime, and carbonate precipitation of heavy metals in industrial effluent (element entry); the carbonate equilibria are in the carbon chapter
    NaHCOX3NaX++HCOX3X\ce{NaHCO3 -> Na^+ + HCO3^-}
    sodium bicarbonate dosing for alkalinity in nitrification and for corrosion control without a pH jump
    NaOCl+HX2OHOCl+NaX++OHX\ce{NaOCl + H2O -> HOCl + Na^+ + OH-}
    sodium hypochlorite dosing, typically 12.5 percent available chlorine; the sodium stays; the chlorine chapter carries the chemistry
    NaX++SOX4X2NaSOX4X\ce{Na^+ + SO4^2- <=> NaSO4^-}
    the outer sphere ion pair; it is negligible in fresh water and matters in reverse osmosis concentrate and brine, where it lowers the free sulfate activity and so raises the sulfate a scaling index will tolerate before barite or gypsum appears
    2NaCl+2HX2O2NaOH+ClX2(g)+HX2(g)\ce{2 NaCl + 2 H2O -> 2 NaOH + Cl2 (g) + H2 (g)}
    the chlor-alkali cell: every sodium reagent a plant buys, caustic soda, hypochlorite, soda ash, starts as salt, and the sodium arrives in the water with whatever anion it was paired with. This is why sodium is the counter-ion of the whole treatment chemical inventory and why it accumulates in a recycled loop
    NaCl+HX2ONaOCl+HX2(g)\ce{NaCl + H2O -> NaOCl + H2 (g)}
    on-site hypochlorite generation by electrolysis of softened brine; the hydrogen is vented and both the sodium and the chloride stay in the treated water, so the salinity cost of on-site generation is the same as that of delivered hypochlorite. No salt consumption figure was read

    4 · Role in treatment

    as a problem
    taste
    sodium salts taste salty or soda like above thresholds that depend on the anion
    WHO: above about 200 mg/L unacceptable taste; EPA: 30 to 60 mg/L is the threshold for taste sensitive individuals, with individual thresholds from about 30 to 460 mg/L
    dietary sodium for restricted patients
    water at 20 mg/L gives about 40 mg/day, small beside a 2 to 8 g/day diet but not for people limited to 500 mg/day
    EPA guidance level 20 mg/L for those individuals, not to be extrapolated to the population; the US requires reporting of sodium to health authorities
    softener sodium
    ion exchange softening trades every calcium and magnesium for two sodium
    WHO: domestic softeners can give over 300 mg/L; hard water of 300 mg/L as CaCO₃ fully softened adds 138 mg/L sodium by the stoichiometry
    sodicity of irrigation water and reclaimed water
    sodium exchanges onto clay, dispersing soil structure and cutting infiltration; the effect is worse at low salinity
    FAO 29 Table 1: with SAR 0 to 3, no restriction above ECw 0.7 dS/m and severe below 0.2; the thresholds rise with SAR (3 to 6: 1.2 and 0.3; 6 to 12: 1.9 and 0.5; 12 to 20: 2.9 and 1.3; 20 to 40: 5.0 and 2.9 dS/m); sodium toxicity to sensitive crops by surface irrigation: SAR below 3 none, 3 to 9 slight to moderate, above 9 severe; sprinkler: below 3 meq/L none, above 3 slight to moderate
    2NaX++XCaXNaX2+CaX2+\ce{2 Na^+ + XCa -> XNa2 + Ca^2+}
    X is a soil clay exchange site; two sodium replace one calcium, which is why the sodium adsorption ratio and not the sodium concentration governs, and why the same sodium level is harmless in a calcium rich water and destroys infiltration in a soft one. Gypsum dosing runs the exchange backwards
    salinity from sodium reagents
    every sodium chemical dosed (hypochlorite, caustic, soda ash, bicarbonate, sulfite, aluminate, silicate, brine) leaves its sodium in the water or the effluent
    the element entry: whatever sodium industry adds stays dissolved and leaves as salinity; ZDHC will limit TDS in textile effluent for this reason
    corrosion and aggressiveness of sodium waters
    sodium bicarbonate waters low in calcium do not form a protective carbonate film; high chloride and sulfate sodium waters raise corrosion rates
    EU DWD: water should not be aggressive or corrosive, and demineralised or softened water may need calcium and magnesium salts added
    sodium hydroxide and hypochlorite hazards
    caustic burns, heat of dilution, hypochlorite decomposition to chlorate
    chlorine chapter for hypochlorite storage
    as a reagent
    sodium hydroxide (caustic soda)
    strong base for pH elevation, metal hydroxide precipitation, membrane cleaning, boron rejection in second pass reverse osmosis, regeneration of anion resins and activated alumina
    NaOHNaX++OHX\ce{NaOH -> Na^+ + OH-}
    50 percent solution freezes near 12 C, 25 percent is the usual winter strength (general practice); no sludge and no hardness, unlike lime
    sodium carbonate (soda ash)
    removes non-carbonate (permanent) hardness after lime softening, precipitates heavy metals as carbonates, raises alkalinity
    NaX2COX3+CaX2+CaCOX3(s)+2NaX+\ce{Na2CO3 + Ca^2+ -> CaCO3 (s) + 2 Na^+}
    lime soda softening (MWH chapter 22); the element entry names soda ash for softening and for metal precipitation
    sodium bicarbonate
    alkalinity supplement for nitrification (7.14 g as CaCO₃ per g N, nitrogen chapter) and for corrosion control
    NaHCOX3NaX++HCOX3X\ce{NaHCO3 -> Na^+ + HCO3^-}
    gentle, self limiting near pH 8.3
    sodium chloride brine
    regenerant for sodium form cation exchangers (softeners) and chloride form anion exchangers (nitrate, perchlorate); feed for on-site hypochlorite generation (hydrogen chapter)
    RX2Ca+2NaCl2RNa+CaClX2\ce{R2Ca + 2 NaCl -> 2 RNa + CaCl2}
    spent brine disposal is the environmental cost of ion exchange
    sodium hypochlorite
    disinfectant and oxidant, 10 to 16 percent commercial strength
    NaOCl+HX2OHOCl+NaX++OHX\ce{NaOCl + H2O -> HOCl + Na^+ + OH-}
    chlorine chapter
    sodium sulfite, bisulfite, metabisulfite and thiosulfate
    dechlorination and oxygen scavenging
    NaX2SOX3+HOClNaX2SOX4+HCl\ce{Na2SO3 + HOCl -> Na2SO4 + HCl}
    chlorine and oxygen chapters; 1.46 parts NaHSO3 or 1.34 parts Na2S2O5 per part chlorine; the chlorine chapter of this book carries the same reaction with sulfur dioxide and sulfite; the sulfur is oxidised from S(IV) to S(VI) and the chlorine reduced to chloride, and an overdose goes on to consume dissolved oxygen at four parts sulfite per part oxygen
    sodium aluminate, sodium silicate, sodium nitrate, sodium fluoride, sodium chlorite
    coagulant aid and alkaline aluminium source; corrosion inhibitor and coagulant aid; electron acceptor for sewer odour control; fluoridation; chlorine dioxide precursor
    NaAlOX2+2HX2OAl(OH)X3(s)+NaX++OHX\ce{NaAlO2 + 2 H2O -> Al(OH)3 (s) + Na^+ + OH-}
    each under its own element; the sodium is the common residue; sodium aluminate is the one coagulant that raises alkalinity instead of consuming it, one equivalent of hydroxide per aluminium, which is why it is paired with alum in soft water

    5 · Removal and control

    reverse osmosis
    membrane rejection of Na⁺ with Cl⁻; the process that desalinates seawater and brackish water
    EPA secondary standards guidance: distillation, reverse osmosis and electrodialysis are effective for chloride, TDS and other inorganics but fairly expensive and may be impractical for small systems
    Efficiency
    rejection above 99 percent for seawater membranes (general, not from a source read)
    Interferences
    scaling by calcium carbonate and sulfate in the concentrate; boron and CO₂ pass (boron and carbon chapters)
    electrodialysis and electrodialysis reversal
    sodium migrates through cation membranes under a direct current
    brackish water; EPA names it with reverse osmosis and distillation
    Efficiency
    not quantified
    distillation and thermal desalination
    sodium stays in the brine
    multistage flash and multiple effect plants of the Gulf; the marine discharge specification exempts their brine (ADS 23)
    Efficiency
    essentially complete
    cation exchange in hydrogen form (demineralisation)
    strong acid resin in H+ form takes Na⁺ and releases acid, followed by an anion bed; regenerated with acid
    RH+NaX+RNa+HX+\ce{RH + Na^+ -> RNa + H+}
    boiler feed and process water (MWH chapter 16); sodium leakage sets the mixed bed polishing need
    Efficiency
    to µg/L in mixed beds (general)
    conventional treatment and softening
    none; sodium form softening adds sodium and lime softening leaves it
    Efficiency
    nil
    sodicity management for irrigation
    not removal but correction: gypsum or calcium chloride raises calcium, lowering SAR; blending with low sodium water
    FAO 29 evaluates SAR with electrical conductivity
    Efficiency
    not applicable

    6 · Analytics

    methodstandarddetection limitnote
    flame atomic absorption or flame emissionStandard Methods 3111 B; 3500-Na B (flame emission); ISO 9964-1 and 9964-32 µg/L by flame AAS (WHO)the classical methods; ionisation suppression with potassium
    ICP-OESEPA 200.7; Standard Methods 3120 B; ISO 1188540 µg/L by ICP-AES (WHO)sodium is among the routine ICP analytes
    ion chromatography, cationsStandard Methods 4110 (anions) with cation columns; ISO 14911not readgives sodium, potassium, ammonium, calcium and magnesium together, the SAR set
    SAR calculationFAO 29 Figure 1not applicableSAR equals sodium divided by the square root of half the sum of calcium and magnesium, all in meq/L; adjusted SAR corrects for calcium precipitation with bicarbonate
    Sampling pitfalls
    Sodium is the easiest ion to contaminate and the hardest to lose: sweat, glass leaching, sodium containing preservatives and detergents raise it. Use plastic bottles rinsed with the sample; acidify with nitric acid only if metals share the bottle. Report the anion balance; sodium is often calculated by difference in old data and is then only as good as the other ions.

    7 · Regulatory limits

    Limits change, and many are set locally. Treat these as the published values to start from, not as your compliance target: check the standard in force at your site and the numbers written into your own permit.

    drinking water
    bodylimitnote
    WHO GDWQ 4th ed. with addenda (2022)no guideline no firm conclusions on sodium in drinking water and hypertension, so no health based guideline; above 200 mg/L unacceptable taste; assessment 1993
    EU DWD 2020/2184200 mg/LAnnex I Part C indicator parameter
    US EPAnot regulated no primary or secondary standard; 2003 drinking water advisory recommends 30 to 60 mg/L for taste (not enforceable, a guideline for States) and keeps the 20 mg/L guidance level for people restricted to 500 mg/day sodium, not to be extrapolated to the whole population; sodium results are reported to the State health authority
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set sodium and salinity are not BAT 12 parameters; the BAT conclusions require monitoring of salts among the relevant pollutants in the waste water stream inventory
    US EPA 40 CFR 133.102, secondary treatmentnot set no federal sodium or TDS effluent limit; salinity limits are permit specific
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)not set
    region-dependent; marine discharge only
    no sodium, chloride or TDS row; desalination brine is exempt from the specification
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewerTDS 2000; chloride 1000 mg/L
    region-dependent; sewer discharge
    Tables A₁ and A₂; sodium itself is not listed, these two rows bracket it
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), total dissolved solidssample and report only mg/LTable 3; salt used in wet processing or formed by neutralisation is not removed by a standard effluent plant, so TDS is reported ahead of a future limit
    irrigationFAO Irrigation and Drainage Paper 29 (1985), Table 1SAR below 3 none; 3 to 9 slight to moderate; above 9 severe (surface irrigation, sensitive crops); sprinkler below 3 meq/L none, above 3 slight to moderate SAR and meq/Linfiltration is evaluated from SAR and conductivity together; usual range of sodium in irrigation water 0 to 40 meq/L and SAR 0 to 15

    8 · Health and environmental effects

    Toxicity
    Essential; adults need about 500 mg/day and Western diets supply 2 to 8 g/day, so drinking water at 20 mg/L (about 40 mg/day) is a minor source (WHO). Acute effects only from gross overdoses of salt; infants with gastrointestinal fluid loss are vulnerable to hypernatraemia. The link between sodium and hypertension is established for diet but no firm conclusion can be drawn for drinking water sodium, hence no guideline (WHO). EPA's 20 mg/L guidance protects people on 500 mg/day diets.
    Bioaccumulation
    Not applicable; regulated by the kidney.
    Ecotoxicity
    No US EPA aquatic criterion for sodium; salinity and chloride criteria apply. In soil the effect is physical: sodic dispersion of clay and loss of infiltration (FAO 29).

    Flags

    • The WHO drinking water surveys are US data from the 1960s to 1980s; the EPA survey is from about 2001.
    • Ion exchange stoichiometry and regenerant doses are cited to MWH chapter 16 from memory of the text, not re-read.
    • Reverse osmosis rejection and mixed bed sodium leakage are general practice, not from sources read.
    • The sodium added per unit hardness (0.46 mg per mg CaCO₃) and per mg NaOH (0.58) are computed from atomic weights here.
    • Abu Dhabi has no sodium limit in either medium; the sewer TDS and chloride rows are quoted as the bracket; other GCC states not read.

    Gaps

    • No sewage or industrial effluent sodium survey was read; the ZDHC TDS reporting requirement stands in for textile.
    • No membrane rejection, resin capacity or brine volume figures are quoted.
    • The WHO chapter 10 acceptability text on sodium and TDS was not read; the fact sheets stand in.
    • The sodium content of reclaimed water for irrigation and the adjusted SAR calculation were not transcribed from FAO 29.
    • Other GCC discharge standards were not read; none of the Abu Dhabi documents limits sodium directly.
    • The chlor-alkali, on-site hypochlorite, sodium aluminate and soil exchange equations are written as the mass balances behind statements the sources make in words; no cell efficiency, salt consumption or soil exchange constant was read.

    Sources

    WHO Guidelines for Drinking-water Quality, 4th ed. incorporating the first and second addenda (2022), chapter 12 chemical fact sheet, Sodium (pp. 462 to 463)
    WHO, Sodium in Drinking-water, background document for development of WHO Guidelines for Drinking-water Quality, WHO/SDE/WSH/03.04/15 (2003; text of 1996)
    US EPA, Drinking Water Advisory: Consumer Acceptability Advice and Health Effects Analysis on Sodium, EPA 822-R-03-006 (February 2003), executive summary and occurrence section
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Annex I Parts B and C
    US EPA, Secondary Drinking Water Standards: Guidance for Nuisance Chemicals
    Commission Implementing Decision (EU) 2016/902 establishing BAT conclusions for common waste water and waste gas treatment/management systems in the chemical sector (CWW), BAT 12 Tables 1 and 2 with footnotes
    40 CFR 133.102, Secondary treatment (BOD5, suspended solids, pH)
    Abu Dhabi Specification ADS 23/2017, Environmental Specifications for Land-Based Liquid Discharges to the Marine Environment (Environment Agency Abu Dhabi), Table 1
    Abu Dhabi Department of Energy, Trade Effluent Control Regulations 2022 (DoE/PD/R01/005, effective 1 January 2022), Schedule A Tables A1, A2 and A4
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), Table 3 conventional parameters and anions
    Ayers, R. S. and Westcot, D. W., Water Quality for Agriculture, FAO Irrigation and Drainage Paper 29 Rev. 1 (1985), Tables 1 and 2 and Figure 1 (SAR)
    US EPA, National Recommended Water Quality Criteria, Aquatic Life Criteria Table
    US EPA, Alternative Disinfectants and Oxidants Guidance Manual, EPA 815-R-99-014 (April 1999), section 2.7.2.2 (sodium hypochlorite) and the dechlorination salts in the chlorine chapter
    MWH, Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 16 (ion exchange: softening, demineralisation, regeneration) and chapter 22 (lime soda softening)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 7 (alkalinity supplements for nitrification)
    Standard Methods for the Examination of Water and Wastewater (online edition), 3111 B, 3120 B, 3500-Na B
    The Element Book, entries for sodium (seawater abundance, salt and soda ash production, conservative ion narrative) (data/elements/Na.json, data/reference/text/Na.json)
    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 6 (ion pairs at high ionic strength)

    Conventions

    Valence electrons are counted by the usual convention: the outer shell for s- and p-block elements, ns and (n-1)d for the d-block, ns, (n-1)d and (n-2)f for the f-block. Lanthanides and actinides are placed in the f-block with no group number. Electrical conductivity is the reciprocal of the printed resistivity. Ionic radii are Shannon effective radii, six-coordinate unless noted. Where a field reads “not in sources” the value was not found; it is a gap, not a zero. Regulatory limits are the published values and change often, so check the standard in force at your site and the numbers written into your own permit before you design to them.

    Data

    Element records, isotopes, radii and the descriptive text come from PubChem (NCBI), the Los Alamos National Laboratory periodic table, IUPAC CIAAW and the IAEA Atomic Mass Data Center. Appearance, thermal conductivity, electrical resistivity, crystal structure, discovery and the origin of each name come from Wikipedia and Periodic-Table-JSON, used under CC BY-SA 4.0. Hazard classifications come from the ECHA C&L inventory via PubChem. Ionic radii follow R. D. Shannon (1976). The water chapters cite their own sources at the foot of each entry, and are written to the level of Snoeyink and Jenkins, Stumm and Morgan, MWH's Water Treatment and Metcalf and Eddy.