Thallium

    group 13 · period 6 · p-block · post-transition metal

    fullThallium is regulated in US drinking water at 2 µg/L (MCLG 0.5 µg/L), one of the tightest inorganic MCLs, because Tl⁺ is more toxic than mercury, cadmium or lead, behaves like potassium in water and in the body, and leaks from sulfide ore processing, smelters, coal combustion and cement works; it has no WHO or EU drinking water value.

    Typical wastewaters

    • zinc electrowinning and sulfide ore processing Tl⁺, the soluble monovalent ion that passes hydroxide precipitation; 100 to 500 mg/L in a zinc process stream removed on manganese dioxide sludge from the electrowinning itself or by oxidative co-precipitation with iron and peroxide
    • lead smelting Tl⁺ in smelter effluent at 12.5 mg/L, treated to below 100 µg/L on manganese dioxide
    • mine closure drainage and process waters Tl⁺ at 50 to 1000 µg/L, taken to below 2 µg/L in a fluidised bed pilot
    • coal combustion and cement manufacture Tl⁺; named with metal smelting by ATSDR as the three main sources of thallium to the environment, medium not specified the cement source is not quantified in the sources read
    • urban stormwater Tl⁺ dissolved, 1 to 14 µg/L in 10 percent of samples
    • electronics, glass and drug factories Tl⁺, the US EPA source list for thallium in drinking water, with leaching from ore processing sites no concentration read

    1 · Identity

    Symbol, number
    Tl, 81
    Oxidation states in water
    +1 as Tl⁺, the state in almost all natural water: a large, weakly hydrated, poorly complexed cation that follows potassium and is not stopped by hydroxide, carbonate or sulfate; +3 as Tl(III), a strong oxidant that hydrolyses to insoluble Tl(OH)₃ and exists in water only where a strong oxidant such as manganese dioxide or permanganate makes it.
    Note
    The element entry covers the metal, TlOH, Tl₂SO₄ and TlCl. The water chemistry is the chemistry of Tl⁺: soluble, mobile and hard to precipitate.

    2 · Occurrence in water

    Natural sources
    Thallium is dispersed in potassium minerals and concentrated in base metal and precious metal sulfides (element entry, Twidwell 2002); waters draining sulfide deposits carry it. Unpolluted fresh water is generally below 1 µg/L; the ATSDR profile reports thallium in tap water in 0.68 percent of samples at an average of 0.89 µg/L.
    Anthropogenic sources
    Coal burning power plants, cement factories and metal smelting are the three main sources named by ATSDR; mining, beneficiation and smelting of sulfide ores, zinc electrowinning and lead smelting effluents (Twidwell 2002); the US EPA lists leaching from ore processing sites and discharge from electronics, glass and drug factories.
    matrixtypical rangenote
    tap water, USA0.89 average where detected µg/L1980s survey datadetected in 0.68 percent of samples
    rivers near mining operations0.7 to 88.3 µg/Lregion-dependent
    urban stormwater1 to 14 µg/Lin 10 percent of samples
    groundwater at hazardous waste sites11 mean where detected µg/L
    contaminated sites, not background
    mine and process wastewater50 to 1000 (closure drainage and process waters); 12.5 mg/L (lead smelter effluent); 100 to 500 mg/L (a zinc process stream) µg/L unless statedsingle sitesfrom the treatment studies annotated by Twidwell and Williams-Beam

    3 · Speciation

    Thallium occurs almost exclusively in natural waters as monovalent Tl⁺, whose compounds, thallous hydroxide included, are relatively soluble, so it is readily transported through aqueous routes (Twidwell 2002). It resembles lead and the alkali metals potassium, rubidium and caesium; it forms weak complexes, does not hydrolyse, and is sorbed mainly by manganese oxides, which can also oxidise it to the insoluble Tl(III) state. Thallium(I) chloride and sulfide are the sparingly soluble Tl(I) solids (element entry).

    conditiondominant speciesnote
    any natural water, pH 4 to 9Tl⁺ free ionnot removed by pH adjustment; passes conventional coagulation
    contact with manganese dioxide or permanganateTl(III) sorbed and precipitated as Tl(OH)₃ or Tl₂O₃ on the oxidethe basis of MnO₂ treatment; sorption on manganese dioxide is effective from pH 4.7 to 8.5 (Twidwell 2002)
    sulfidic waterTl₂S (s)thallium(I) sulfide, the infrared detector material of the element entry; sulfide precipitation is a treatment route
    chloride brinesTlCl (s) crust; TlCl₄⁻ only for Tl(III)the poorly soluble Tl(I) chloride stops acid attack on the metal (element entry)
    Solubility
    Thallous hydroxide is a water soluble strong base (element entry), so unlike lead or zinc thallium cannot be precipitated by lime; TlCl is poorly soluble, Tl₂S insoluble. No solubility products are printed in the sources read.
    Hydrolysis
    Tl⁺ does not hydrolyse in the natural pH range; Tl³⁺ hydrolyses completely to Tl(OH)₃ (general chemistry, from the book entry's description of Tl(III) as a strong oxidant; no constant read).
    Complexation
    Weak; Tl⁺ behaves as a potassium analogue with some affinity for sulfur ligands and for organic matter. No constants read.
    Precipitates
    Tl₂S, TlCl, TlI, and Tl(OH)₃ or Tl₂O₃ on manganese oxide surfaces; thallium co-precipitated on ferric hydroxide with oxidation.
    TlX++ClXTlCl(s)\ce{Tl^+ + Cl^- -> TlCl (s)}
    the one Tl(I) salt of low solubility besides the sulfide; it matters in chloride brines and as the crust that stops acid attacking thallium metal (element entry); it is not a treatment route at microgram per litre thallium and no solubility product was read
    2TlX++HSXTlX2S(s)+HX+\ce{2 Tl^+ + HS^- -> Tl2S (s) + H+}
    sulfide precipitation of Tl(I); the compound is in the element entry; stoichiometry written here, no read source prints it
    TlX3++3OHXTl(OH)X3(s)\ce{Tl^3+ + 3 OH- -> Tl(OH)3 (s)}
    after oxidation of Tl(I) by a strong oxidant such as manganese dioxide or permanganate; Tl(III) is insoluble at any pH above about 2
    TlX++MnOX2(s)+HX2O+HX+Tl(OH)X3(s)+MnX2+\ce{Tl^+ + MnO2 (s) + H2O + H+ -> Tl(OH)3 (s) + Mn^2+}
    the reaction behind manganese dioxide treatment and behind thallium enrichment in natural manganese nodules: the oxide takes two electrons from Tl(I) and the Tl(III) hydrolyses on the surface; effective from pH 4.7 to 8.5 (Twidwell). Written here as the electron balance; the sources read do not resolve whether sorption or oxidation dominates, and no potential was read

    4 · Role in treatment

    as a problem
    not removed by conventional metal precipitation
    Tl⁺ has soluble hydroxide, carbonate and sulfate, so lime, caustic and coagulation leave it in solution
    Twidwell: thallous compounds are relatively soluble so Tl⁺ is readily transported; the problem in zinc and lead plant effluents
    TlX++OHXTlOH(aq)\ce{Tl^+ + OH- -> TlOH (aq)}
    why lime and caustic fail on thallium: thallous hydroxide is a water soluble strong base (element entry), so raising pH gives a dissolved species instead of the filterable hydroxide that lead, zinc, copper and nickel give; thallium has to be oxidised or precipitated as the sulfide instead
    competition with potassium and other cations on resins
    Tl⁺ exchanges like K⁺ and Cs⁺
    EPA: competing ions in water may affect treatment run lengths
    very low limits
    the US MCL of 2 µg/L and a Hunan provincial discharge limit of 5 µg/L sit near the detection limits of routine ICP-MS
    the Hunan figure is from a search summary, not a read source, and is flagged
    as a reagent
    none in treatment
    thallium is never dosed

    5 · Removal and control

    activated alumina
    sorption of thallium on alumina; the US BAT for the MCL
    BAT with ion exchange (57 FR 31776, 1992); also a small system compliance technology
    Efficiency
    greater than 95 percent (EPA, 55 FR 30370)
    Interferences
    competing ions shorten runs
    cation exchange
    Tl⁺ exchanges onto strong acid cation resin
    RNa+TlX+RTl+NaX+\ce{RNa + Tl^+ -> RTl + Na^+}
    BAT; point of use ion exchange is a small system option; the exchange written in the usual resin notation for a sodium form strong acid bed (R one exchange site), which is also why potassium, the ion Tl^+ imitates, is the competitor that ends a run
    Efficiency
    greater than 90 percent (EPA)
    Interferences
    hardness and potassium compete; treatment is not known to be a limiting concern for the current MCL
    sorption on manganese dioxide
    electrolytically formed or biogenic MnO₂ sorbs and oxidises Tl(I); manganese dioxide sludge from zinc electrowinning removes thallous ions from zinc process waters and lead smelting effluent
    TlX++MnOX2(s)+HX2O+HX+Tl(OH)X3(s)+MnX2+\ce{Tl^+ + MnO2 (s) + H2O + H+ -> Tl(OH)3 (s) + Mn^2+}
    pH 4.7 to 8.5; lead smelting effluent treated from 12.5 mg/L to below 100 µg/L (Jibiki 1995 via Twidwell); fine, minus 400 mesh electrolytic MnO2 at about 1 g/L; the reaction is written as the two electron transfer to the oxide with the Tl(III) hydrolysing on the surface, and it consumes acid and releases dissolved manganese; Twidwell reports the performance without a stoichiometry
    Efficiency
    from 12.5 mg/L to below 100 µg/L
    Interferences
    gold in solution strengthens sorption in the cited carbon study; high zinc, acid, hot streams (75 g/L zinc, pH 2.5 to 4.5, 40 to 75 C) are not effectively treated
    oxidative co-precipitation with iron and peroxide
    hydrogen peroxide oxidises Tl(I), which co-precipitates with ferric hydroxide
    TlX++HX2OX2+2HX+TlX3++2HX2O\ce{Tl^+ + H2O2 + 2 H+ -> Tl^3+ + 2 H2O}
    100 to 500 mg/L thallium with 12.5 g/L iron and 100 cm3 of 30 percent H2O2 per litre for 15 minutes gave 1 to 20 mg/L (Twidwell); a fluidised bed column pilot took closure drainage and process waters of 50 to 1000 µg/L to below 1.7 and below 2 µg/L; the oxidation step written as the electron balance, one mole of peroxide per mole of thallium, after which Tl(III) hydrolyses and is swept down with the ferric hydroxide; Twidwell gives the doses and results, not the equation
    Efficiency
    to 1 to 20 mg/L from hundreds; to below 2 µg/L from 50 to 1000 µg/L in the pilot
    Interferences
    reagent cost at high concentrations
    sulfide precipitation
    Tl₂S is insoluble where the hydroxide is not
    2TlX++HSXTlX2S(s)+HX+\ce{2 Tl^+ + HS^- -> Tl2S (s) + H+}
    sulfide reagents as for mercury and lead; not detailed in the sources read
    Efficiency
    not quoted
    Interferences
    excess sulfide, sludge handling

    6 · Analytics

    methodstandarddetection limitnote
    ICP-MSEPA 200.8; ISO 17294-2EPA 200.8 Table 7 MDL 0.3 µg/L scanning modemass 205; the compliance method for the 2 µg/L MCL
    graphite furnace atomic absorptionEPA 200.9not readEPA has considered lowering the thallium practical quantitation limit on analytical grounds (EPA 2003)
    Sampling pitfalls
    Acidify with nitric acid; Tl⁺ is stable in solution and does not sorb strongly to bottle walls, but particulate thallium on manganese oxide flocs is lost if the sample is filtered before digestion. Report total and dissolved separately in mine waters.

    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
    US EPA NPDWR0.002 mg/LMCL; MCLG 0.0005 mg/L; sources listed as leaching from ore processing sites and discharge from electronics, glass and drug factories; BAT activated alumina and ion exchange
    EU DWD 2020/2184not set thallium is not an Annex I parameter
    WHO GDWQ 4th ed. with addenda (2022)no guideline thallium has no chemical fact sheet in chapter 12 as far as the sheets read this session show; the full chapter 12 index was not re-read
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set thallium is not among the BAT 12 parameters
    US EPA effluent guidelines (40 CFR)not regulated no thallium limitation in the parts read (423, 433, 440); thallium is a priority pollutant addressed in permits
    Abu Dhabi ADS 23/2017 (marine outfall) and DoE Trade Effluent Control Regulations 2022 (sewer)not set
    region-dependent; other GCC states not read
    thallium is not a listed parameter in either table
    industry thresholds
    sectorbodylimitnote
    textileZDHC Wastewater Guidelines v₂.1 (2022)not set thallium is not a ZDHC parameter

    8 · Health and environmental effects

    Toxicity
    More toxic to humans than mercury, cadmium, lead, copper or zinc (Twidwell 2002); thallium(I) sulfate was a rodenticide banned for household use (element entry); the US MCLG of 0.5 µg/L reflects effects on hair loss, blood chemistry and the nervous system at low doses. Smokers excrete about twice the thallium of non smokers (ATSDR).
    Bioaccumulation
    Bioconcentration factors from 11.7 in mussels to 1430 in Atlantic salmon muscle; thallium is taken up by vegetables from contaminated soil, the main exposure route for the public (ATSDR 1992).
    Ecotoxicity
    No US EPA aquatic life criterion or EU EQS was read for thallium; the bioconcentration data are the ecotoxicological signal in the sources read.

    Flags

    • The ATSDR occurrence figures are 1980s Contract Laboratory Program and survey data quoted in the 1992 profile; a 2024 draft profile exists and was not read.
    • The treatment concentrations are from individual studies annotated by Twidwell and Williams-Beam (2002), not from operating plants.
    • The WHO 'no guideline' row is inferred from the absence of a thallium fact sheet among those read, not from a WHO statement; the chapter 12 index was not re-read.
    • The sulfide and Tl(III) hydroxide equations are written here from the element entry's compound list; no read source prints them, and the MnO₂ oxidation stoichiometry is deliberately not written.
    • The Hunan provincial discharge limit of 5 µg/L (2014) is from a search summary and is not cited as a source.
    • The GCC tables list no thallium; other GCC states not read.

    Gaps

    • No source read gives thallium in seawater, in surface water as a survey range, in municipal wastewater or in cement plant effluent as a number; the cement source is named by ATSDR but not quantified.
    • Solubility products of TlCl, Tl₂S and Tl(OH)₃ and the Tl(I) to Tl(III) redox potential are not in the sources read.
    • The WHO position on thallium and any EU national values were not read.
    • EPA 200.9 and other method detection limits were not read.
    • Aquatic toxicity values (EC₅₀, chronic criteria) were not sourced.
    • The mechanism on MnO₂ (sorption versus oxidation) is debated in the literature and not resolved by the sources read.
    • No surface complexation or co-precipitation stoichiometry was read for thallium on ferric hydroxide; only the peroxide oxidation step is written for that row.

    Sources

    US EPA, National Primary Drinking Water Regulations (table of MCLs and MCLGs, inorganic chemicals and radionuclides)
    US EPA, Water Treatment Technology Feasibility Support Document for Chemical Contaminants, EPA 815-R-03-004 (June 2003), section 5 Thallium
    ATSDR, Toxicological Profile for Thallium (1992), chapter 5 Potential for human exposure
    Twidwell, L. G. and Williams-Beam, C., Potential technologies for removing thallium from mine and process wastewater: an abbreviated annotation of the literature, European Journal of Mineral Processing and Environmental Protection 2 (2002) 1 to 10
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Article 11, Annex I Part B, Annex II Part D and Annex III
    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
    Abu Dhabi Specification ADS 23/2017, Environmental Specifications for Land-Based Liquid Discharges to the Marine Environment (Environment Agency Abu Dhabi), Table 1
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), Table 2 heavy metals and Table 4 sludge parameters
    US EPA Method 200.8, Revision 5.4 (1994), Determination of trace elements in waters and wastes by ICP-MS, Table 7 (method detection limits)
    ISO 17294-2:2023, Water quality. Application of ICP-MS. Part 2: Determination of selected elements including uranium isotopes
    The Element Book, element entry and reference text for Tl (data/elements/Tl.json, data/reference/text/Tl.json)

    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.