Magnesium

    group 2 · period 3 · s-block · alkaline earth metal

    fullMagnesium is the second cation of hardness, the harder half to soften because it needs pH above 10.5 and a second dose of lime, the metal of brucite and struvite scale and of deliberate struvite recovery, a possibly protective nutrient in drinking water that WHO declines to set a guideline for, and, as magnesium hydroxide slurry, a safer substitute for lime and caustic in pH control.

    Typical wastewaters

    • digester supernatant and sludge dewatering liquors Mg²⁺ with ammonium and phosphate released in digestion, precipitating struvite MgNH₄PO₄ above about pH 8
    • desalination brine Mg²⁺ concentrated from 1290 mg/L in seawater; magnesium compounds are recovered from seawater and brines
    • reverse osmosis concentrate Mg²⁺ concentrated with the hardness; Mg(OH)₂ scaling at high pH held off with antiscalant
    • ion exchange softener regenerant Mg²⁺ and Ca²⁺ in spent NaCl brine
    • textile dyeing (magnesium sulfate mordant) Mg²⁺ with sulfate from the mordant

    1 · Identity

    Symbol, number
    Mg, 12
    Oxidation states in water
    +2 only, as the strongly hydrated Mg²⁺ ion. It hydrolyses only above pH 9, precipitates as Mg(OH)₂ (brucite) above about pH 10.5, forms carbonate and sulfate ion pairs in hard and saline water, and unlike calcium does not precipitate as a simple carbonate from fresh water. The element entry has the tightly bound hydration and the chlorophyll centre.
    Note
    The element entry carries the ores, the metal, seawater and brine extraction and the industrial magnesia uses. This chapter is magnesium as hardness, as scale, as struvite and as a reagent. The carbonate equilibria are in the carbon chapter; calcium carbonate softening is in the calcium chapter with the shared equations kept there; ammonium and phosphate point here for struvite.

    2 · Occurrence in water

    Natural sources
    Dissolution of dolomite, magnesite, olivine and serpentine and of magnesium in sedimentary rocks, seepage and runoff from soils (WHO hardness document); seawater at about 1290 mg/L, the third most abundant ion after chloride and sodium, and evaporite brines (element entry). Magnesium is present in natural groundwater usually at lower concentrations than calcium, from negligible to about 50 mg/L and rarely above 100 mg/L (WHO).
    Anthropogenic sources
    Magnesium hydroxide and magnesium oxide dosed for pH control and as alkalinity, magnesium sulfate and chloride in industrial processes (the element entry lists the sulfate as a dye mordant), desalination brine, dolomitic lime, magnesium in digester supernatant and dewatering liquors where it meets ammonium and phosphate.
    matrixtypical rangenote
    groundwaternegligible to about 50 mg/Lrarely above 100 mg/L; calcium is usually higher, so calcium contributes more to hardness
    drinking water, hardness (calcium plus magnesium)10 to 500 mg/L as CaCO3the range in drinking water; below 60 mg/L soft, 60 to 120 moderately hard, 120 to 180 hard, above 180 very hard
    drinking water, magnesium intake2.3 (soft water areas) to 52.1 (hard water areas) mg/day from waterreported adult intakes from water; food supplies over 80 percent of the total
    seawater1290 mg/Lsingle figureoceanic abundance figure, Jefferson Lab via PubChem, quoted in the element entry; magnesium compounds are recovered from seawater and brines
    municipal wastewater and digester liquornot read no survey read; magnesium in sludge liquors is what precipitates struvite with the ammonium and phosphate released in digestion

    3 · Speciation

    Magnesium is Mg²⁺ across the pH range of natural water, with MgSO₄, MgHCO₃⁺ and MgCO₃ ion pairs in mineralised and sea water. It hydrolyses to MgOH⁺ only above pH 9 and precipitates as Mg(OH)₂ above about pH 10.5, a pH unit higher than calcium carbonate, which is why magnesium hardness needs the excess lime and the higher pH of the softening process. Magnesium carbonate does not precipitate from fresh water (it is far more soluble than calcite and forms hydrated salts only in brines), so magnesium hardness is removed as hydroxide, not carbonate. Where ammonium and phosphate are both present, as in anaerobic digester liquors, magnesium precipitates as struvite, MgNH₄PO₄ hexahydrate, above about pH 8 (Metcalf and Eddy chapter 15).

    conditiondominant speciesnote
    natural water, pH 6 to 9Mg²⁺; MgSO₄ and MgHCO₃⁺ ion pairs in hard waterhalf the hardness in dolomitic and seawater influenced supplies
    lime softening, pH 10.5 to 11.3Mg(OH)₂ (s)the magnesium removal condition; calcium carbonate has already precipitated at 10.3
    digester supernatant and dewatering liquor, pH above 8MgNH₄PO₄.6H₂O (struvite) on pipe walls, pumps and centrifugesCO₂ loss raises the pH and triggers it
    seawater and reverse osmosis concentrateMg²⁺ with MgSO₄ ion pairs; Mg(OH)₂ if the concentrate is dosed alkalinebrucite scaling is a risk in alkaline second pass reverse osmosis
    magnesium hydroxide slurry dosingMg(OH)₂ particles dissolving slowly to Mg²⁺ and OH-cannot overshoot pH 9 to 10 because the solid stops dissolving there
    Solubility
    Magnesium chloride, sulfate, nitrate and bicarbonate are freely soluble; magnesium hydroxide is sparingly soluble and controls magnesium above pH 10.5; magnesium carbonate is much more soluble than calcium carbonate and does not control magnesium in fresh water; struvite is sparingly soluble at alkaline pH. No solubility product is quoted because none was read this session.
    Hydrolysis
    Mg²⁺ is a very weak acid; MgOH⁺ forms only above pH 9 and Mg(OH)₂ precipitates above 10.5. Magnesium oxide hydrates to the hydroxide in water.
    Complexation
    Sulfate, bicarbonate and carbonate ion pairs; magnesium binds phosphate and organic ligands more weakly than calcium; in seawater about 10 percent of magnesium is paired with sulfate (Stumm and Morgan chapter 6, from the chapter). Constants not quoted.
    Precipitates
    Mg(OH)₂ brucite (lime softening, caustic dosing, alkaline scaling); MgNH₄PO₄.6H₂O struvite (digester liquors, deliberate recovery); MgCO₃ hydrates and dolomite only in brines and over geological time; magnesium silicate in high silica boiler and cooling water (not read this session).
    MgX2++2OHXMg(OH)X2(s)\ce{Mg^2+ + 2 OH- -> Mg(OH)2 (s)}
    pH above about 10.5; the magnesium removal reaction of lime softening and of caustic precipitation; 4.12 mg of hardness as CaCO3 per mg magnesium by the molar masses
    Mg(HCOX3)X2+2Ca(OH)X22CaCOX3(s)+Mg(OH)X2(s)+2HX2O\ce{Mg(HCO3)2 + 2 Ca(OH)2 -> 2 CaCO3 (s) + Mg(OH)2 (s) + 2 H2O}
    magnesium carbonate hardness needs two moles of lime per mole: one to convert the bicarbonate to carbonate (which precipitates with the calcium added) and one to raise the pH for the hydroxide; excess lime softening (MWH chapter 22)
    MgSOX4+Ca(OH)X2Mg(OH)X2(s)+CaSOX4\ce{MgSO4 + Ca(OH)2 -> Mg(OH)2 (s) + CaSO4}
    magnesium non-carbonate hardness: lime precipitates the magnesium but leaves an equivalent of calcium non-carbonate hardness, which soda ash then removes (sodium and carbon chapters)
    MgX2++NHX4X++POX4X3+6HX2OMgNHX4POX46HX2O(s)\ce{Mg^2+ + NH4^+ + PO4^3- + 6 H2O -> MgNH4PO4.6H2O (s)}
    struvite, pH above about 8, where magnesium, ammonium and phosphate coincide; unwanted on digester lines and deliberate in a fluidised bed reactor dosed with magnesium chloride or hydroxide (Metcalf and Eddy chapter 15)
    Mg(OH)X2(s)+2HX+MgX2++2HX2O\ce{Mg(OH)2 (s) + 2 H+ -> Mg^2+ + 2 H2O}
    magnesium hydroxide slurry neutralising acid effluent or supplying alkalinity; two equivalents of alkalinity per mole, self limiting near pH 9 to 10 (element entry: substitutes for lime in pH control)
    2RNa+MgX2+RX2Mg+2NaX+\ce{2 RNa + Mg^2+ -> R2Mg + 2 Na^+}
    ion exchange softening removes magnesium with calcium on the sodium form resin (R is the resin site); adds 0.46 mg sodium per mg hardness as CaCO3 (sodium chapter)
    MgO(s)+HX2OMg(OH)X2(s)\ce{MgO (s) + H2O -> Mg(OH)2 (s)}
    magnesium oxide hydrates to the hydroxide in water; this is what a magnesia slurry becomes before it neutralises anything, and it is why magnesia and magnesium hydroxide are interchangeable as reagents
    MgO(s)+2COX2+HX2OMgX2++2HCOX3X\ce{MgO (s) + 2 CO2 + H2O -> Mg^2+ + 2 HCO3^-}
    remineralisation of desalinated or softened water with magnesia or half burnt dolomite dissolved by carbon dioxide; it adds magnesium and two equivalents of alkalinity per mole and leaves no sludge, unlike caustic; WHO recommends restoring calcium and magnesium without printing this stoichiometry
    MgX2++HX4SiOX4MgSiOX3(s)+2HX++HX2O\ce{Mg^2+ + H4SiO4 -> MgSiO3 (s) + 2 H+ + H2O}
    magnesium silicate scale in high silica boiler, cooling and membrane concentrate water; the reaction releases acid, so it runs harder as pH and magnesium rise, and magnesium is the strongest catalyst of silica polymerisation; the book's silicon water chapter carries the silica solubility ceiling of 120 to 150 mg/L that sets when this starts

    4 · Role in treatment

    as a problem
    hardness: soap consumption and scale
    calcium and magnesium react with soap and deposit carbonate and hydroxide scale in kettles, heaters, boilers, membranes and distribution mains
    WHO: hardness above about 200 mg/L may cause scale deposition and increased soap consumption; soft water below 100 mg/L may be corrosive; aesthetic acceptability, not health
    the harder half to soften
    magnesium removal needs pH 10.5 to 11.3 and excess lime, then recarbonation; sludge volume rises
    US enhanced softening rules credit a plant that removes at least 10 mg/L of magnesium hardness as CaCO₃ with meeting the TOC precursor removal requirement (40 CFR 141.135), because Mg(OH)₂ floc adsorbs organic carbon
    struvite scaling
    digested sludge liquors release ammonium and phosphate; CO₂ stripping in pipes and centrifuges raises pH and struvite crystallises on walls and impellers
    Metcalf and Eddy chapter 15; the cure is controlled precipitation and recovery upstream, or iron dosing to bind phosphate
    brucite and magnesium silicate scale
    high pH concentrate in reverse osmosis, boilers and cooling towers precipitates magnesium hydroxide and silicate
    acid or antiscalant dosing; second pass reverse osmosis at pH 10 to 11 for boron must run on low hardness permeate (boron chapter)
    laxative effect with sulfate
    magnesium and sulfate both above about 250 mg/L
    WHO hardness document; usually in new consumers of a high sulfate groundwater; sulfur chapter
    remineralisation of desalinated water
    reverse osmosis and thermal distillate carry almost no calcium or magnesium and are corrosive and flat tasting
    EU DWD Annex I: calcium and magnesium salts could be added and minimum concentrations could be established; WHO: consider adding calcium and magnesium to reach the concentrations the population received before, given the debated cardiovascular evidence
    lime sludge
    every mg of magnesium removed becomes Mg(OH)₂ sludge, gelatinous and hard to dewater, unlike CaCO₃
    MWH chapter 22 (from the chapter)
    as a reagent
    magnesium hydroxide slurry for pH control and alkalinity
    slow dissolving base that neutralises acid effluent, buffers nitrification and digestion, and precipitates metals without the overshoot risk of caustic or the sludge of lime
    Mg(OH)X2(s)+2HX+MgX2++2HX2O\ce{Mg(OH)2 (s) + 2 H+ -> Mg^2+ + 2 H2O}
    self limiting near pH 9 to 10; environmental use leads US consumption of magnesia and magnesium hydroxide (element entry); dose from acidity titration
    magnesium for struvite recovery
    magnesium chloride or hydroxide dosed to digester liquor precipitates struvite in a controlled reactor, recovering phosphorus and some nitrogen as a slow release fertiliser
    MgX2++NHX4X++POX4X3+6HX2OMgNHX4POX46HX2O(s)\ce{Mg^2+ + NH4^+ + PO4^3- + 6 H2O -> MgNH4PO4.6H2O (s)}
    magnesium to phosphate molar ratio a little above 1, pH 8 to 9 by aeration or caustic (Metcalf and Eddy chapter 15); phosphorus, not nitrogen, limits the yield
    magnesium in enhanced softening
    freshly precipitated Mg(OH)₂ adsorbs natural organic matter, removing disinfection by-product precursors
    40 CFR 141.135(a)(3): removing at least 10 mg/L of magnesium hardness as CaCO3 is an alternative compliance criterion
    dolomitic lime and magnesium oxide for remineralisation
    half burnt dolomite or magnesia dissolved with CO₂ adds calcium, magnesium and alkalinity to desalinated water
    MgO(s)+2COX2+HX2OMgX2++2HCOX3X\ce{MgO (s) + 2 CO2 + H2O -> Mg^2+ + 2 HCO3^-}
    EU DWD note on conditioning demineralised water; WHO on restoring calcium and magnesium (general practice for the reagent choice)
    magnesium sulfate as a nutrient
    trace nutrient for biological treatment of industrial wastewater short of magnesium
    general practice, not from a source read

    5 · Removal and control

    excess lime softening
    lime to pH 10.5 to 11.3 precipitates Mg(OH)₂ with CaCO₃; soda ash for non-carbonate hardness; recarbonation with CO₂ and filtration
    Mg(HCOX3)X2+2Ca(OH)X22CaCOX3(s)+Mg(OH)X2(s)+2HX2O\ce{Mg(HCO3)2 + 2 Ca(OH)2 -> 2 CaCO3 (s) + Mg(OH)2 (s) + 2 H2O}
    two moles of lime per mole of magnesium carbonate hardness plus 30 to 70 mg/L excess; split treatment softens part of the flow to the magnesium end point and blends (MWH chapter 22)
    Efficiency
    magnesium to about 10 mg/L as CaCO₃ (40 mg/L total hardness residual is typical, from the chapter)
    Interferences
    temperature, silica, organic matter; gelatinous Mg(OH)₂ sludge
    ion exchange softening
    sodium form strong acid resin takes Mg²⁺ and Ca²⁺ and releases two Na⁺ each; regenerated with brine
    2RNa+MgX2+RX2Mg+2NaX+\ce{2 RNa + Mg^2+ -> R2Mg + 2 Na^+}
    domestic and industrial softeners; complete removal of hardness while capacity lasts; the sodium load is in the sodium chapter
    Efficiency
    to below 1 mg/L as CaCO₃
    Interferences
    iron and manganese foul the resin; brine disposal
    nanofiltration and reverse osmosis
    divalent ions are rejected almost completely; nanofiltration passes much of the sodium chloride and takes the hardness
    membrane softening; antiscalant against CaCO3, CaSO4 and Mg(OH)2 in the concentrate
    Efficiency
    above 90 percent for magnesium by nanofiltration (general, not from a source read)
    Interferences
    scaling
    caustic precipitation in industrial effluent
    sodium hydroxide to pH 11 precipitates Mg(OH)₂ from brines, pickling liquors and desalination concentrate
    MgX2++2OHXMg(OH)X2(s)\ce{Mg^2+ + 2 OH- -> Mg(OH)2 (s)}
    magnesium recovery from brine in the element entry (electrolysis feed); high pH precipitation is the same reaction
    Efficiency
    to the brucite solubility at the pH reached
    struvite precipitation
    removes magnesium with ammonium and phosphate; used for phosphorus, the magnesium is the reagent
    equation above
    Efficiency
    not applicable to magnesium
    Interferences
    calcium competes to form calcium phosphate

    6 · Analytics

    methodstandarddetection limitnote
    EDTA titration (hardness) and calculationStandard Methods 2340 C (total hardness), 3500-Mg B (magnesium by calculation from hardness minus calcium); ISO 6059about 1 mg/L as CaCO₃titration at pH 10 with Eriochrome Black T; magnesium is total hardness minus calcium hardness (calcium titrated at pH 12 to 13 with murexide)
    flame atomic absorptionStandard Methods 3111 B; ISO 7980not readlanthanum added to suppress phosphate and aluminium interference
    ICP-OES and ICP-MSEPA 200.7; Standard Methods 3120 B; ISO 11885; ISO 17294-2not readroutine; hardness reported as 2.497 times calcium plus 4.118 times magnesium in mg/L as CaCO₃
    ion chromatography, cationsISO 14911not read
    Sampling pitfalls
    Acidify with nitric acid to keep magnesium and calcium in solution when the sample warms or degasses; an unacidified hard water sample loses calcium carbonate, and a struvite forming liquor loses magnesium, on the bench. Filter digester liquors immediately for dissolved magnesium. Report hardness units clearly: mg/L as CaCO₃ is not mg/L magnesium (factor 4.12), and German, French and English degrees are still met.

    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), hardnessno guideline not of health concern at levels found in drinking water; may affect acceptability; insufficient data to propose minimum or maximum mineral concentrations; assessment 1993, revised 2011; drinking water can be a contributor to calcium and magnesium intake and stabilisation of demineralised water is always necessary before distribution
    WHO GDWQ, acceptabilityabove about 200 scale; below 100 corrosion mg/L as CaCO3hardness above about 200 mg/L may cause scale deposition and higher soap consumption; soft water below 100 mg/L may have low buffering capacity and be corrosive (hardness background document)
    EU DWD 2020/2184not set no parametric value for hardness, calcium or magnesium; Annex I Part C says water should not be aggressive or corrosive and that calcium and magnesium salts could be added to demineralised or softened water, with minimum concentrations of calcium, magnesium or TDS that could be established
    US EPAnot regulated no primary or secondary standard for magnesium or hardness; hardness appears among the effects of the 500 mg/L TDS secondary standard
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set magnesium is not among the BAT 12 parameters
    US EPA 40 CFR 133.102, secondary treatmentnot set no federal magnesium or hardness effluent limit
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)not set
    region-dependent; marine discharge only
    no magnesium row in Table 1
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewernot set
    region-dependent; sewer discharge
    no magnesium row; TDS 2000 mg/L (Table A₁) is the nearest constraint
    industry thresholds
    sectorbodylimitnote
    textileZDHC Wastewater Guidelines v₂.1 (2022)not set magnesium is not a ZDHC parameter

    8 · Health and environmental effects

    Toxicity
    Essential: the fourth most abundant cation in the body, needed by hundreds of enzymes; intake 250 to 350 mg/day (element entry); food supplies over 80 percent and drinking water 2 to 52 mg/day depending on hardness (WHO). Low magnesium status is implicated in hypertension, insulin resistance and cardiovascular disease, and there is evidence, debated and not proving causality, of a protective effect of water magnesium or hardness on cardiovascular mortality, with benefits where observed at about 10 mg/L magnesium and above (WHO hardness document). Magnesium with sulfate above about 250 mg/L each is laxative. Not toxic in water (element entry).
    Bioaccumulation
    Not applicable.
    Ecotoxicity
    No US EPA aquatic criterion for magnesium; hardness raises the toxicity thresholds of metals, which is why the metal criteria are hardness dependent (aluminium criterion by pH, hardness and DOC in the criteria table).

    Flags

    • Lime softening stoichiometry, pH end points, residual hardness and the Mg(OH)₂ sludge remark are cited to MWH chapter 22 from memory of the text, not re-read.
    • The struvite conditions and the magnesium to phosphate ratio are from Metcalf and Eddy chapter 15 likewise.
    • Nanofiltration rejection and the magnesium nutrient use are general practice, not from sources read.
    • The conversion factors (4.12 mg CaCO₃ per mg Mg, 2.497 per mg Ca) are computed from molar masses here.
    • No Abu Dhabi document limits magnesium in either medium; other GCC states not read.

    Gaps

    • No solubility products for brucite, magnesite or struvite are quoted; Stumm and Morgan and Metcalf and Eddy have them.
    • No survey of magnesium in sewage, digester liquors or industrial effluents was read.
    • No lime dose, sludge production or struvite reactor performance figures beyond the stoichiometry are quoted.
    • The WHO 2009 monograph on calcium and magnesium in drinking water (public health significance) was not read; the 2011 hardness document cites it.
    • Magnesium silicate scaling and magnesium in cooling water chemistry are not sourced here.
    • Other GCC discharge standards were not read.
    • The magnesia remineralisation and magnesium silicate stoichiometries are written here; WHO states the principle of restoring magnesium and the silicon chapter of the book carries the silica chemistry, neither prints these equations.

    Sources

    WHO Guidelines for Drinking-water Quality, 4th ed. incorporating the first and second addenda (2022), chapter 12 chemical fact sheet, Hardness (pp. 408 to 409)
    WHO, Hardness in Drinking-water, background document for development of WHO Guidelines for Drinking-water Quality, WHO/HSE/WSH/10.01/10/Rev/1 (2011), sections 1 to 4
    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
    40 CFR 141.135, Treatment technique for control of disinfection byproduct precursors (Step 1 TOC removal table, enhanced coagulation target pH)
    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
    US EPA, National Recommended Water Quality Criteria, Aquatic Life Criteria Table
    MWH, Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 16 (ion exchange softening) and chapter 22 (lime soda softening, magnesium hydroxide precipitation, sludge)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 15 (struvite formation and recovery from sidestreams)
    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 6 (ion pairs in seawater) and chapter 7 (magnesium hydroxide and carbonate solubility)
    Standard Methods for the Examination of Water and Wastewater (online edition), 2340 Hardness, 3500-Mg, 3111 B, 3120 B
    The Element Book, entries for magnesium (seawater abundance, brine and seawater recovery, magnesium hydroxide as a lime substitute, dietary intake) (data/elements/Mg.json, data/reference/text/Mg.json)
    The Element Book, water chapter for silicon (data/water/Si.json): amorphous silica solubility ceiling, magnesium silicate scale and silica removal on magnesium hydroxide

    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.