Sulfur

    group 16 · period 3 · p-block · polyatomic nonmetal

    fullSulfur is the sulfate of every water (an EU indicator parameter and US secondary standard at 250 mg/L), the sulfide that stinks, corrodes sewers and poisons fish at micrograms per litre, the sulfite that dechlorinates and scavenges oxygen, and the sulfuric acid that is the cheapest pH reagent in the plant.

    Typical wastewaters

    • leather tanning sulfide (HS⁻ and H₂S) from lime and sulfide dehairing liquors, with chromium; BAT-AEL below 1 mg/L for direct and indirect discharge the US pretreatment standard (40 CFR 425.15) allows 24 mg/L daily maximum to sewer
    • textile dyeing with sulfur dyes sulfide easily released, below 1 mg/L BAT-AEL for direct and indirect discharge ZDHC also limits sulfite in textile effluent (2, 0.5, 0.2 mg/L by level)
    • wool scouring sulfide, mass limited per 1000 kg of wool with phenol and chromium
    • mine drainage and industrial brines sulfate from pyrite oxidation, capped by gypsum at 1.5 to 2 g/L after lime treatment; barium reaches lower
    • municipal sewage (septic sewers) sulfate reduced to sulfide in the slime layer; H₂S strips to the headspace and is oxidised to sulfuric acid on the sewer crown
    • dechlorinated effluent and boiler blowdown sulfite from sulfur dioxide or bisulfite dechlorination and from oxygen scavenging, oxidised to sulfate by dissolved oxygen
    • reverse osmosis concentrate sulfate concentrated past gypsum and barite solubility; recovery limited by scaling
    In the ledger's plant and process records, discharged by: Cleaning-in-place and disinfection (Food and beverage) · Speciality inorganic explosives (lead azide, lead trinitroresorcinate, lead picrate) (Chemicals) · Fruit and vegetables (Food and beverage) · Lower olefins (steam cracking) (Chemicals) · Silicones (polydimethylsiloxane) (Chemicals) · Speciality inorganic pigments (iron oxide, chromium oxide, CIC, zinc sulphide, lithopone) (Chemicals) · Viscose fibres (staple, filament, lyocell) (Chemicals) · Dairies (Food and beverage) · Fish and shellfish processing (Food and beverage) · Meat processing (Food and beverage) · Wine production (Food and beverage) · Cyanides (sodium and potassium cyanide) (Chemicals) · Ethylbenzene and styrene (Chemicals) · Phenol (cumene route) (Chemicals) · Phosphoric acid (wet process) (Chemicals) · Sulphuric acid (Chemicals) · Abrasion peeling (Food and beverage) · Belt blanching with air cooling (Food and beverage) · Belt blanching with water cooling (Food and beverage) · Blanching (Food and beverage) · Brewing (Food and beverage) · Dried fruit (Food and beverage) · Drum blancher with countercurrent water cooling (Food and beverage) · Dry caustic peeling (Food and beverage) · Enzymatic peeling (Food and beverage) · Frozen fruit and vegetables (Food and beverage) · Fruit juice (Food and beverage) · Fruit preserves (Food and beverage) · Grain milling (Food and beverage) · Heat-treated and frozen vegetables (Food and beverage) · Heat-treated fruit (Food and beverage) · Knife peeling (Food and beverage) · Oilseed processing and vegetable oil refining (Food and beverage) · Olive oil processing and refining (Food and beverage) · Peeling (Food and beverage) · Pickling of vegetables (Food and beverage) · Potato crisps (Food and beverage) · Potato fries (Food and beverage) · Potatoes (Food and beverage) · Ready meals containing predominantly fruit and vegetables (Food and beverage) · Starch production (Food and beverage) · Steam blanching with air cooling (Food and beverage) · Steam peeling – batch process (Food and beverage) · Steam peeling – continuous process (Food and beverage) · Sugar manufacturing (Food and beverage) · Sugar refining (Food and beverage) · Tomatoes (Food and beverage) · Vegetable drying (Food and beverage) · Vegetable juice (Food and beverage) · Wet caustic peeling (Food and beverage) · Base metal ores (Cu, Ni, Pb, Sn, Zn) (Mining) · Chemical treatment (Mining) · Industrial minerals (potash, salt, kaolin, magnesite and others) (Mining) · Iron ore and other metalliferous ores (Co, Cr, Mn, Mo, V, W) (Mining) · Leaching (Mining) · Management of extractive waste influenced water (Mining) · Precious metal ores (Au, Ag, Pt): gold and silver extraction (Mining) · Diazotisation and azo coupling (Pharmaceuticals) · Esterification (Pharmaceuticals) · N-acylation (Pharmaceuticals) · Nitration (Pharmaceuticals) · Sulphonation (Pharmaceuticals) · Sulphonation with SO3 (Pharmaceuticals)

    1 · Identity

    Symbol, number
    S, 16
    Oxidation states in water
    +6 as sulfate SO₄²⁻ (and HSO₄⁻ below pH 2), the stable form in oxic water; +4 as sulfite SO₃²⁻ and bisulfite HSO₃⁻ (dechlorination and oxygen scavenging reagents, unstable in air); -2 as hydrogen sulfide H₂S, bisulfide HS⁻ and metal sulfides in anoxic water; 0 as elemental sulfur from partial oxidation of sulfide; +2 as thiosulfate S₂O₃²⁻ (dechlorination reagent). Organic sulfur in proteins and surfactants.
    Note
    The element entry covers brimstone, sour gas and the acid industry. This chapter is the redox ladder in water: sulfate down to sulfide in the absence of oxygen, sulfide back to sulfate (by way of sulfuric acid in a sewer crown) when air returns, and the sulfite step that treatment plants buy by the tonne.

    2 · Occurrence in water

    Natural sources
    Dissolution of gypsum, anhydrite and other sulfate minerals and oxidation of pyrite give sulfate; the highest sulfate is in groundwater from natural sources (WHO). Sulfide comes from microbial reduction of sulfate in anaerobic groundwater, sediments and sulfur springs, and from volcanic and geothermal sources.
    Anthropogenic sources
    Industrial wastes and atmospheric deposition of sulfur dioxide (acid rain); sulfate added by alum and ferric sulfate coagulants and by sulfuric acid dosing (treated water in Ontario carried 22.5 mg/L sulfate against 12.5 mg/L raw); mine drainage from pyrite oxidation; tannery (sulfide dehairing), sulfur dye, pulp and petroleum wastes carry sulfide; dechlorination and boiler blowdown carry sulfite and sulfate.
    matrixtypical rangenote
    fresh water, generalabout 20 mg/L sulfateregion-dependent compilationsrivers 0 to 630 mg/L (highest in Belgium and Mexico), lakes 2 to 250 mg/L, groundwater 0 to 230 mg/L
    rivers, western Canada1 to 3040 mg/L sulfateregion-dependentmost below 580 mg/L
    rain1.0 to 3.8 (Canada); about 6 (central Europe annual mean) mg/L sulfate1980s dataatmospheric sulfur dioxide
    US public water suppliesbelow 1 to 770, median 4.6 mg/L sulfate3 percent of supplies above 250 mg/L
    seawaterabout 2700 mg/L sulfateWHO figure; PubChem gives 905 mg/L as sulfur, which is the same value (905 times 96 over 32 is about 2715 mg/L sulfate)
    fresh water, undissociated hydrogen sulfideup to 500 µg/Lsingle maximummaximum reported in the USA; sulfide is noticeable in some groundwaters depending on source rock and microorganisms

    3 · Speciation

    In oxic water sulfur is sulfate, a conservative anion that pairs weakly with calcium and magnesium and precipitates only as gypsum above about 1.5 to 2 g/L or as barium sulfate. Where oxygen runs out and organic carbon is present, sulfate reducing bacteria turn it to sulfide; at pH 7.4 about one third of that sulfide is dissolved H₂S gas and the rest HS⁻, and the odour, toxicity and corrosivity follow the H₂S fraction, which rises as pH falls (pKa₁ about 7.0). Free sulfide is capped by iron: FeS forms wherever ferrous iron is available. Air or chlorine oxidises sulfide back through elemental sulfur to sulfate, and sulfur oxidising bacteria on a sewer crown make sulfuric acid out of it. Sulfite, dosed as sulfur dioxide, bisulfite or metabisulfite, is oxidised to sulfate by chlorine or dissolved oxygen within seconds to minutes.

    conditiondominant speciesnote
    oxic water, any pH above 2SO₄²⁻, ion pairs CaSO₄ (aq) and MgSO₄ (aq)conservative through most treatment; removed only by membranes, ion exchange or precipitation
    anoxic water with organic carbon, pH 6 to 8H₂S (aq) and HS⁻ in roughly equal parts near pH 7, FeS (s) where iron is present, elemental sulfur at the oxic boundarysulfide is present as S²⁻ in appreciable amounts only above pH 10
    acid mine water, pH below 3HSO₄⁻ and SO₄²⁻, iron and aluminium sulfate complexes, jarosite and schwertmannite precipitatesthe acid is sulfuric acid from pyrite oxidation
    dechlorinated or bisulfite dosed waterHSO₃⁻ and SO₃²⁻ transiently, then SO₄²⁻excess sulfite consumes dissolved oxygen
    Solubility
    Sulfate is capped by gypsum (CaSO₄.2H₂O), about 2 g/L as the salt in pure water at 25 C, which sets the sulfate ceiling of lime treated acid mine drainage and the scaling limit of reverse osmosis concentrate (Stumm and Morgan chapter 7, from the chapter, not re-read); barium sulfate is far less soluble. Hydrogen sulfide is a soluble gas that strips readily. Metal sulfides (FeS, CuS, ZnS, NiS, PbS, HgS) are among the least soluble solids in water, which is the basis of sulfide precipitation.
    Hydrolysis
    H₂S dissociates with pKa₁ near 7.0 at 25 C, so the toxic, odorous, volatile molecule dominates below pH 7 and HS⁻ above it; the second dissociation lies above pH 12, so S²⁻ is negligible in treatment (WHO gives the one third H₂S at pH 7.4 figure). Sulfurous acid: SO₂ hydrates to HSO₃⁻ and SO₃²⁻ with pKa values near 1.9 and 7.2 (Stumm and Morgan chapter 3, from the chapter, not re-read).
    Complexation
    Sulfate forms weak ion pairs with Ca²⁺, Mg²⁺ and Fe²⁺ and complexes Al³⁺ and Fe³⁺ in acid water; bisulfide complexes copper, mercury and other soft metals, which is why sulfide precipitates can carry dissolved polysulfide metal at very high sulfide.
    Precipitates
    Gypsum and anhydrite, barite BaSO₄, ettringite in lime treated sulfate water, jarosite and schwertmannite in acid mine drainage; FeS, CuS, ZnS, NiS, PbS in sulfidic water and in sulfide precipitation; elemental sulfur.
    HX2SHSX+HX+\ce{H2S <=> HS^- + H+}
    pKa1 about 7.0 at 25 C; at pH 7.4 about one third of sulfide is H2S (WHO background document)
    SOX4X2+2CHX2OHX2S+2HCOX3X\ce{SO4^2- + 2 CH2O -> H2S + 2 HCO3^-}
    microbial sulfate reduction in anaerobic water with organic carbon (CH2O as generic organic matter); the stoichiometry from Stumm and Morgan chapter 8 (from the chapter, not re-read); WHO states the process
    2HX2S+OX22S(s)+2HX2O\ce{2 H2S + O2 -> 2 S (s) + 2 H2O}
    partial oxidation by air, chemical and by sulfur bacteria, at the oxic boundary; WHO: sulfide is readily oxidised to sulfate in well aerated water and biologically to elemental sulfur
    HSX+2OX2SOX4X2+HX+\ce{HS^- + 2 O2 -> SO4^2- + H+}
    complete oxidation in aerated water; on a sewer crown sulfur oxidising bacteria produce the acid that attacks concrete (Metcalf and Eddy chapter 2, from the chapter, not re-read)
    CaSOX42HX2O(s)CaX2++SOX4X2+2HX2O\ce{CaSO4.2H2O (s) <=> Ca^2+ + SO4^2- + 2 H2O}
    gypsum solubility, about 2 g/L at 25 C; the sulfate ceiling of lime treatment and a reverse osmosis scalant

    4 · Role in treatment

    as a problem
    taste and laxative effect of sulfate
    sodium, calcium and magnesium sulfate taste thresholds 250 to 1000 mg/L; osmotic laxative effect at 1000 to 1200 mg/L
    WHO recommends notifying health authorities above 500 mg/L; no health based guideline
    rotten egg odour and taste of sulfide
    H₂S is detected in water at 0.05 to 0.1 mg/L, sulfides at about 0.2 mg/L
    usually a groundwater problem; oxidised away by aeration or chlorination (WHO)
    sewer crown corrosion and odour
    sulfate reduced to sulfide in the slime layer and sediment of a septic sewer; H₂S strips into the headspace and is oxidised on the moist crown to sulfuric acid by sulfur oxidising bacteria, which dissolves concrete and attacks iron
    the mechanism as in Metcalf and Eddy chapter 2; control by oxygen, nitrate, iron salts or oxidants (from the chapter, not re-read)
    corrosion of distribution systems by sulfate
    sulfate raises the aggressiveness of water to metals and attacks cement and concrete
    the EU DWD note on sulphate reads that the water should not be corrosive; WHO says sulfate may contribute to corrosion of distribution systems
    gypsum and barium sulfate scaling
    sulfate concentrates in reverse osmosis reject and cooling water past the gypsum and barite solubility
    antiscalants and recovery limits; figures not read this session
    oxygen depletion by excess sulfite
    sulfite dosed beyond the chlorine demand reduces dissolved oxygen
    the book's chlorine entry: four parts sulfite per part oxygen; lowers pH
    sulfide toxicity to fish and treatment biology
    H₂S is acutely toxic to aquatic life at micrograms per litre and inhibits nitrifiers and methanogens
    US EPA chronic criterion 2.0 µg/L
    biogas hydrogen sulfide
    sulfate in the digester feed is reduced to H₂S that corrodes engines and must be scrubbed
    qualitative; no figures read
    as a reagent
    sulfuric acid for pH control and membrane feed conditioning
    cheapest strong acid; lowers pH ahead of coagulation, converts bicarbonate to carbon dioxide ahead of reverse osmosis to prevent calcium carbonate scale, regenerates cation exchangers, neutralises alkaline effluent
    HX2SOX4+2HCOX3XSOX4X2+2COX2+2HX2O\ce{H2SO4 + 2 HCO3^- -> SO4^2- + 2 CO2 + 2 H2O}
    adds one sulfate per mole of acid, which the discharge sulfate limit must absorb; the element entry: about 90 percent of sulfur is consumed as sulfuric acid
    dechlorination with sulfur dioxide, sodium sulfite, bisulfite and metabisulfite
    sulfite reduces free and combined chlorine to chloride and is oxidised to sulfate
    SOX3X2+HOClSOX4X2+ClX+HX+\ce{SO3^2- + HOCl -> SO4^2- + Cl^- + H+}
    about 1 part SO2 per part chlorine in practice (0.9 stoichiometric); 1.46 parts sodium bisulfite or 1.34 parts metabisulfite per part chlorine; sulfur dioxide with HOCl gives SO4^2-, Cl^- and 3 H+ per mole; the same reagents remove chlorine ahead of polyamide reverse osmosis membranes (equations and doses as in the book's chlorine entry)
    sodium thiosulfate for dechlorination of samples and small flows
    thiosulfate is oxidised to sulfate by chlorine
    NaX2SX2OX3+4HOCl+HX2O2NaHSOX4+4HCl\ce{Na2S2O3 + 4 HOCl + H2O -> 2 NaHSO4 + 4 HCl}
    laboratory sample bottles and small plants; slower than sulfite (the book's chlorine entry, Metcalf and Eddy chapter 12)
    sulfite as boiler oxygen scavenger
    sulfite reacts with dissolved oxygen to sulfate
    2SOX3X2+OX22SOX4X2\ce{2 SO3^2- + O2 -> 2 SO4^2-}
    Standard Methods 4500-SO3 notes sulfite in boilers and feedwater treated for dissolved oxygen control and in effluents dechlorinated with sulfur dioxide
    sulfite, bisulfite and sulfur dioxide as reductant for chromium(VI)
    sulfite reduces chromate to Cr³⁺ at low pH before hydroxide precipitation
    2CrOX4X2+3HSOX3X+7HX+2CrX3++3SOX4X2+5HX2O\ce{2 CrO4^2- + 3 HSO3^- + 7 H+ -> 2 Cr^3+ + 3 SO4^2- + 5 H2O}
    acid pH, then lime or caustic to pH 8 to 9; the CWW BREF chapter on chemical reduction names sulfite and ferrous sulfate; the equation is the electron balance
    sodium sulfide and hydrosulfide for metal precipitation
    metal sulfides are far less soluble than hydroxides, so sulfide polishing reaches lower residual copper, nickel, zinc, lead and mercury than hydroxide precipitation
    NiX2++HSXNiS(s)+HX+\ce{Ni^2+ + HS^- -> NiS (s) + H+}
    the CWW BREF lists sulfide precipitation among its techniques; excess sulfide must be controlled because of H2S release (Metcalf and Eddy chapter 6 on metal precipitation, from the chapter, not re-read)
    sulfate salts as coagulants and algaecide
    alum, ferrous and ferric sulfate and copper sulfate deliver their cation and leave sulfate behind
    the sulfate rise in treated water noted by WHO (12.5 to 22.5 mg/L in Ontario)
    iron salts for sulfide control in sewers and digesters
    ferrous or ferric iron precipitates sulfide as FeS
    FeX2++HSXFeS(s)+HX+\ce{Fe^2+ + HS^- -> FeS (s) + H+}
    dosed to force mains and digester feed; the equation as in the book's iron entry

    5 · Removal and control

    sulfide: aeration and stripping
    H₂S is volatile below pH 7; forced draft or packed tower aeration strips it and oxidises the remainder
    2HX2S+OX22S(s)+2HX2O\ce{2 H2S + O2 -> 2 S (s) + 2 H2O}
    lower pH favours stripping, higher pH favours oxidation in solution; off gas odour must be scrubbed
    Efficiency
    not quoted
    Interferences
    elemental sulfur turbidity; HS⁻ does not strip
    sulfide: chemical oxidation with chlorine, chlorine dioxide, ozone or permanganate
    oxidation to sulfur at low dose and to sulfate at full dose
    HX2S+4ClX2+4HX2OHX2SOX4+8HCl\ce{H2S + 4 Cl2 + 4 H2O -> H2SO4 + 8 HCl}
    chlorine dioxide, ozone and permanganate all oxidise sulfides; chloramines cannot (EPA oxidant manual); the full oxidation needs 8.3 mg Cl2 per mg H2S from the stoichiometry, partial oxidation to sulfur one quarter of that
    Efficiency
    to below the 0.05 mg/L odour threshold in practice
    Interferences
    sulfur colloids if underdosed; chlorine demand of the water
    sulfide: catalytic aeration with manganese salts and biological oxidation
    manganese catalyses air oxidation of sulfide in tannery effluent; sulfur bacteria oxidise sulfide to sulfur and sulfate in biofilters
    the tanning BAT conclusions prescribe precipitation and catalytic oxidation with manganese salts for indirect discharges
    Efficiency
    sulphide below 1 mg/L BAT-AEL
    sulfate: reverse osmosis and nanofiltration
    divalent sulfate is rejected almost completely by both
    recovery limited by gypsum and barite scaling; antiscalant dosing
    Efficiency
    not quoted in the sources read
    Interferences
    scaling
    sulfate: lime and barium precipitation
    lime precipitates gypsum down to its solubility ceiling and, with aluminium, ettringite; barium salts precipitate BaSO₄ to low residuals
    BaX2++SOX4X2BaSOX4(s)\ce{Ba^2+ + SO4^2- -> BaSO4 (s)}
    mine water and industrial brines; gypsum leaves 1.5 to 2 g/L sulfate, so lime alone cannot meet a 250 mg/L limit
    Efficiency
    gypsum ceiling; barium to well below the drinking water value
    Interferences
    barium toxicity and cost
    sulfate: biological sulfate reduction
    sulfate reducing bacteria fed with organic carbon or hydrogen convert sulfate to sulfide, which is stripped or precipitated as metal sulfide and sulfur
    SOX4X2+2CHX2OHX2S+2HCOX3X\ce{SO4^2- + 2 CH2O -> H2S + 2 HCO3^-}
    anaerobic reactor; generates alkalinity, useful for acid mine drainage
    Efficiency
    not quoted
    Interferences
    H₂S handling
    sulfite: air oxidation
    residual sulfite is oxidised to sulfate by dissolved oxygen
    2SOX3X2+OX22SOX4X2\ce{2 SO3^2- + O2 -> 2 SO4^2-}
    fast in aerated water
    Efficiency
    complete
    Interferences
    oxygen depletion in the receiving water if the dose is large

    6 · Analytics

    methodstandarddetection limitnote
    sulfate by ion chromatographyISO 10304-1; Standard Methods 4110 B and C; EPA 300ISO 10304-1 lower limit 0.1 mg/LZDHC lists these for sulfate
    sulfate by turbidimetry (barium chloride)Standard Methods 4500-SO₄ Enot readgravimetric barium sulfate methods apply above 10 mg/L (WHO cites ISO 1990)
    sulfide by methylene blue colorimetryStandard Methods 4500-S₂ D; ISO 10530ISO 10530 range 0.04 to 1.5 mg/L; WHO quotes 0.1 to 20 mg/L for the methylene blue methodZDHC and the tanning BAT use it; iodometric 4500-S₂ F for higher levels
    hydrogen sulfide by acid displacement and GC-FPDno numbered standard readabout 0.25 mg S/L; 0.06 mg/L reported for a similar method (WHO)for water, sewage and effluents 0 to 2 mg/L
    sulfite by iodometry or ion chromatographyStandard Methods 4500-SO₃ B; ISO 10304-3not readsulfite oxidises in air during sampling; analyse at once
    total sulfur by ICP-OESISO 11885; EPA 200.7 lists sulfur among analytes only by wavelengthnot readrarely used; sulfate by IC is the routine
    Sampling pitfalls
    Sulfide is lost from the bottle within minutes by volatilisation and oxidation: fill without headspace and fix with zinc acetate and sodium hydroxide at the tap (Standard Methods 4500-S₂ sample handling, not re-read). Sulfite oxidises in air; titrate on site. Sulfate is stable but a chlorinated or bisulfite dosed sample keeps reacting, so dechlorinated effluent should be sampled after the reaction is complete.

    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), sulfateno guideline not of health concern at levels found; laxative effect at 1000 to 1200 mg/L; health authorities should be notified of sources above 500 mg/L; taste; corrosion of distribution systems; assessment 2003
    WHO GDWQ, hydrogen sulfideno guideline not of health concern at levels found; taste and odour threshold 0.05 to 0.1 mg/L H₂S, about 0.2 mg/L sulfides; assessment 1993
    EU DWD 2020/2184, sulphate250 mg/LAnnex I Part C indicator parameter, note: the water should not be corrosive; uncertainty of measurement 15 percent (Annex III); no sulfide or sulfite parameter
    US EPA, sulfate250 mg/LNational Secondary Drinking Water Regulation, non enforceable; salty taste; no primary standard for sulfate or sulfide
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set sulfate, sulfide and sulfite are not BAT 12 parameters
    EU tanning BAT conclusions (Decision 2013/84/EU), sulphidebelow 1 mg/LBAT-AEL for direct and for indirect discharge, monthly average of 24 hour composite samples; total chromium in the same tables
    EU textiles BAT conclusions (Decision 2022/2508), sulphide easily releasedbelow 1 mg/Ldirect and indirect discharge, dyeing with sulphur dyes
    US EPA 40 CFR 425.15, leather tanning PSES, sulfide24 mg/L daily maximumpretreatment standard for discharge to sewer, subpart A; with total chromium 12 and 8 mg/L and pH not less than 7.0
    US EPA 40 CFR 410.12, textile mills wool scouring BPT, sulfide0.20 daily maximum; 0.10 30-day average kg per 1000 kg of wool
    production normalised, not a concentration
    mass based; phenol and total chromium at 0.10 and 0.05
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD), sulfide0.1 mg/L
    region-dependent; marine discharge only
    Table 1; no sulfate value in the table
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewersulphate 1000; sulphide 1 mg/L
    region-dependent; sewer discharge
    Table A₂ (sulphate as SO₄, sulphide as S)
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), sulfidetextile 0.5 foundational, 0.05 progressive, 0.01 aspirational; leather 1, 0.5, 0.2 mg/Lmethods ISO 10530, SM 4500-S₂ D, E, G or I
    textileZDHC Wastewater Guidelines v₂.1 (2022), sulfite2 foundational; 0.5 progressive; 0.2 aspirational mg/Ltextile only; ISO 10304-3, SM 4500-SO₃ C
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), sulfatesample and report only mg/Lno limit value; ISO 10304-1, SM 4500-SO₄ E to G

    8 · Health and environmental effects

    Toxicity
    Sulfate: no level causing adverse effects identified; laxative at 1000 to 1200 mg/L without diarrhoea, dehydration or weight loss; average daily intake about 500 mg mostly from food (WHO). Hydrogen sulfide: high acute inhalation toxicity, eye irritation at 15 to 30 mg/m₃ in air, but a harmful oral dose from drinking water is not credible because taste and odour give it away (WHO). Sulfite is a food additive; no drinking water value.
    Bioaccumulation
    Not applicable; sulfur is an essential element taken up as sulfate by plants and algae (the element entry).
    Ecotoxicity
    US EPA aquatic life criterion for sulfide as hydrogen sulfide: chronic 2.0 µg/L in fresh and salt water (1986), no acute value; sulfate has no criterion but high sulfate depresses osmotic tolerance in freshwater biota (not quantified in the sources read).

    Flags

    • The H₂S pKa₁ (about 7.0), the sulfurous acid pKa values, the gypsum solubility and the sulfate reduction stoichiometry are cited to Stumm and Morgan chapters from memory, not re-read; WHO supports the pKa with its one third H₂S at pH 7.4 statement.
    • The crown corrosion mechanism is cited to Metcalf and Eddy chapter 2 without re-reading.
    • The chlorine demand of 8.3 mg Cl₂ per mg H₂S is computed from the stoichiometry written here; the EPA manual states that chlorine oxidises sulfides without printing the dose.
    • The chromate reduction by sulfite and the nickel sulfide precipitation are electron and charge balances; the CWW BREF names the techniques without printing equations.
    • The sulfate occurrence figures are compilations of the 1980s quoted by WHO in 2004.
    • The wool scouring limit is mass based (kg per 1000 kg) and cannot be compared with concentration limits.
    • Abu Dhabi values cover two media (marine sulfide 0.1 mg/L; sewer sulfate 1000 and sulfide 1 mg/L).
    • Sample preservation for sulfide (zinc acetate) is standard practice cited from memory of Standard Methods 4500-S₂.

    Gaps

    • No source read gives sulfide or sulfate in municipal wastewater, tannery, textile or pulp effluent as numbers; only the limits are quoted.
    • Gypsum and barite scaling limits for reverse osmosis and antiscalant doses were not read.
    • Sewer sulfide control doses (oxygen, nitrate, iron, peroxide) were not read; the EPA odour and corrosion design manual could not be opened.
    • Detection limits for the Standard Methods sulfate, sulfide and sulfite methods were not read.
    • Biogas hydrogen sulfide figures were not sourced.
    • Sulfate criteria for aquatic life (state or Canadian) were not read.
    • Other GCC discharge standards (Saudi, Oman, Qatar) were not read.

    Sources

    WHO GDWQ 4th ed. with addenda (2022), chapter 12 fact sheet, Sulfate (p. 466)
    WHO, Sulfate in Drinking-water, background document, WHO/SDE/WSH/03.04/114 (2004), sections 1.3, 2, 3.2 and 6
    WHO GDWQ 4th ed. with addenda (2022), chapter 12 fact sheet, Hydrogen sulfide (p. 412)
    WHO, Hydrogen Sulfide in Drinking-water, background document, WHO/SDE/WSH/03.04/07 (2003), organoleptic properties, environmental fate, analytical methods and environmental levels
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Annex I Parts B and C and Annex III
    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
    Best Available Techniques Reference Document for Common Waste Water and Waste Gas Treatment/Management Systems in the Chemical Sector (CWW BREF 2016), chapter 3 (chemical reduction, chemical precipitation)
    Commission Implementing Decision 2013/84/EU establishing BAT conclusions for the tanning of hides and skins, BAT 10 to 12, BAT 24 and Tables 3 and 4
    Commission Implementing Decision (EU) 2022/2508 establishing BAT conclusions for the textiles industry, BAT-AELs for direct and indirect discharges (OJ L 325, 20.12.2022, pp. 141 to 142)
    40 CFR 425.15, Pretreatment standards for existing sources (PSES), leather tanning and finishing, subpart A (hair pulp, chrome tan, retan-wet finish)
    40 CFR 410.12, Effluent limitations representing BPT, textile mills, subpart A (wool scouring)
    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), Appendix Tables A2 and A4
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), conventional parameters, anions and metals tables and sludge Table 4A
    US EPA, Alternative Disinfectants and Oxidants Guidance Manual, EPA 815-R-99-014 (April 1999), oxidant summaries (sulfide oxidation by ozone, chlorine dioxide and permanganate; chloramines cannot oxidise sulfides)
    US EPA, National Recommended Water Quality Criteria, Aquatic Life Criteria Table (sulfide-hydrogen sulfide, 1986)
    Standard Methods (online edition), 4500-SO4 2- Sulfate (E. turbidimetric method)
    Standard Methods (online edition), 4500-S2- Sulfide (D. methylene blue method, F. iodometric method)
    Standard Methods (online edition), 4500-SO3 2- Sulfite (B. iodometric method)
    ISO 10304-1:2007, Water quality. Determination of dissolved anions by liquid chromatography of ions. Part 1: bromide, chloride, fluoride, nitrate, nitrite, phosphate and sulfate
    ISO 10304-3:1997, Water quality. Determination of dissolved anions by liquid chromatography of ions. Part 3: chromate, iodide, sulfite, thiocyanate and thiosulfate
    ISO 10530:1992, Water quality. Determination of dissolved sulfide. Photometric method using methylene blue
    ISO 11885:2007, Water quality. Determination of selected elements by inductively coupled plasma optical emission spectrometry (ICP-OES)
    US EPA Method 200.7, Revision 4.4 (1994), Determination of metals and trace elements in water and wastes by ICP-AES, Table 1 (wavelengths and instrument detection limits), Table 4 (method detection limits) and Table 5 (argon plasma conditions)
    PubChem element summary for sulfur; estimated oceanic abundance 905 mg/L (PUG View, reference 5, Jefferson Lab)
    The Element Book, layer 1 entry for sulfur (data/elements/S.json and data/reference/text/S.json)
    The Element Book, water chapter for chlorine (data/water/Cl.json), dechlorination reactions and doses
    The Element Book, water chapter for iron (data/water/Fe.json), iron sulfide precipitation
    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 3 (acids and bases: H2S and sulfurous acid), chapter 7 (precipitation: gypsum) and chapter 8 (oxidation and reduction: sulfate reduction)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 2 (hydrogen sulfide in sewers, crown corrosion), chapter 6 (sulfide precipitation of metals) and chapter 12 (dechlorination)
    Crittenden, J. C. et al., MWH's Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 17 (reverse osmosis: sulfate rejection and scaling)

    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.