Carbon

    group 14 · period 2 · p-block · polyatomic nonmetal

    fullCarbon is two of the three master variables of water treatment: inorganic carbon (dissolved CO₂, bicarbonate, carbonate) sets pH, alkalinity, buffering, corrosion and scaling, and organic carbon (TOC, DOC, BOD, COD) is the load that biological treatment removes, the precursor that chlorine turns into trihalomethanes and the parameter that EU, US and every discharge permit regulate; carbon dioxide and activated carbon are also treatment reagents.

    Typical wastewaters

    • municipal sewage biodegradable and refractory organic carbon measured as BOD₅ 110 to 350, COD 250 to 800 and TOC 80 to 260 mg/L, with bicarbonate alkalinity 50 to 200 mg/L as CaCO₃ low to high strength typical composition
    • chemical sector effluent dissolved organic carbon, refractory fraction dominant after biological treatment; TOC 10 to 33 and COD 30 to 100 mg/L as yearly averages, halogenated organics as AOX 0.20 to 1.0 mg/L
    • textile dyeing and finishing and leather tanning organic load measured as BOD₅ and COD (textile 150, 80, 40 and leather 250, 150, 100 mg/L COD by level), halogenated fraction as AOX in textile
    • high strength industrial wastewater and sludge digestion organic carbon converted anaerobically to methane and CO₂ (about 0.35 m₃ methane per kg COD removed); the effluent needs aerobic polishing
    In the ledger's plant and process records, discharged by: Fruit and vegetables (Food and beverage) · Starch production (Food and beverage) · Wine production (Food and beverage) · Brewing (Food and beverage) · Grain milling (Food and beverage) · Oilseed processing and vegetable oil refining (Food and beverage) · Olive oil processing and refining (Food and beverage) · Sugar manufacturing (Food and beverage) · Ethylene dichloride and vinyl chloride monomer (Chemicals) · Phenol (cumene route) (Chemicals) · Ethylbenzene and styrene (Chemicals) · Polyvinyl chloride (suspension and emulsion PVC) (Chemicals) · Urea and UAN (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) · Cheese (Food and beverage) · Dairies (Food and beverage) · Distilled beverages (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) · Ethanol production (Food and beverage) · Fermentation (Food and beverage) · Fish and shellfish processing (Food and beverage) · Frozen fruit and vegetables (Food and beverage) · Fruit juice (Food and beverage) · Fruit preserves (Food and beverage) · Heat-treated and frozen vegetables (Food and beverage) · Heat-treated fruit (Food and beverage) · Knife peeling (Food and beverage) · Maize starch (Food and beverage) · Meat processing (Food and beverage) · Modified (physical/chemical) starches (Food and beverage) · Peeling (Food and beverage) · Pickling of vegetables (Food and beverage) · Potato crisps (Food and beverage) · Potato fries (Food and beverage) · Potato starch (Food and beverage) · Potatoes (Food and beverage) · Ready meals containing predominantly fruit and vegetables (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) · Sweeteners (Food and beverage) · Tomatoes (Food and beverage) · Vegetable drying (Food and beverage) · Vegetable juice (Food and beverage) · Waste water treatment (Food and beverage) · Wet caustic peeling (Food and beverage) · Wheat starch (Food and beverage) · Yeast (Food and beverage) · Yoghurt (Food and beverage) · Gold leaching with cyanide (Mining) · Heap leach pad (Mining) · Halogenation (Pharmaceuticals) · Sulphochlorination with chlorosulphonic acid (Pharmaceuticals) · Sulphonation with SO3 (Pharmaceuticals) · Desizing (Textile) · Easy-care finishing (Textile) · Mothproofing and antimicrobial finishing (Textile)

    1 · Identity

    Symbol, number
    C, 6
    Oxidation states in water
    +4 as dissolved carbon dioxide, carbonic acid, bicarbonate and carbonate (dissolved inorganic carbon, DIC), and as the solid carbonates that scale and dissolve; -4 as methane in anoxic water and digester gas; every state between in dissolved and particulate organic matter, from -3 in methyl groups through 0 in carbohydrate to +3 in carboxylic acids, whose average state sets the ratio of COD to organic carbon; 0 as the activated carbon that adsorbs organics and reduces chlorine.
    Note
    The element entry carries the allotropes, the carbon cycle, CO₂ in the atmosphere and the fossil carbon economy. This chapter is the carbonate system, the organic carbon parameters, the reagents and the limits. Chlorine's by-products are in the chlorine chapter; nitrification's alkalinity demand is in the nitrogen chapter; struvite and calcium carbonate softening chemistry are in the magnesium and calcium chapters, with the carbonate equations kept here.

    2 · Occurrence in water

    Natural sources
    Inorganic carbon enters water from atmospheric CO₂ (about 390 ppm by 2013 in the element entry), from respiration of organic matter in soil, where CO₂ partial pressures reach ten to a hundred times atmospheric, and from dissolution of limestone and dolomite by that CO₂; the result is the bicarbonate alkalinity of nearly all fresh water. Organic carbon comes from the decay of vegetation and algae (humic and fulvic acids, the natural organic matter that colours water and reacts with chlorine) and from soil leaching; groundwater usually carries little (the US rule treats source TOC below 2 mg/L as needing no precursor removal), surface water more.
    Anthropogenic sources
    Sewage and industrial organic loads measured as BOD, COD and TOC; methane from landfills, digesters and anoxic sediments; carbon dioxide dosed for recarbonation and pH control; activated carbon and coke; halogenated organics measured as AOX; carbon dioxide from the burning of fossil carbon, which is acidifying the ocean (element entry).
    matrixtypical rangenote
    surface water, source water TOC2.0 to above 8.0 mg/Lregulatory bands, not a surveythe bands of the US enhanced coagulation table (2 to 4, 4 to 8, above 8 mg/L); source or treated water below 2.0 mg/L is exempt from TOC removal, which is where most groundwater sits
    fresh water, alkalinity0 to above 240 mg/L as CaCO3regulatory bandsthe bands of the same table (0 to 60, 60 to 120, 120 to 240, above 240 mg/L as CaCO₃), which are also the practical range of natural water
    seawater, dissolved inorganic carbon28 mg/Lsingle figureoceanic abundance figure for carbon, Jefferson Lab via PubChem, quoted in the element entry; essentially all bicarbonate and carbonate
    untreated municipal wastewaterBOD₅ 110 to 350; COD 250 to 800; TOC 80 to 260; alkalinity 50 to 200 mg/L (alkalinity as CaCO3)
    textbook typical values, not a survey
    low, medium and high strength typical composition, Metcalf and Eddy 5th ed. Table 3-18, from the chapter and not re-read
    industrial wastewater, chemical sector effluent after treatmentTOC 10 to 33; COD 30 to 100 mg/L
    achievable emission levels, not raw effluent
    the CWW BAT-AEL ranges as yearly averages; the upper ends may reach 100 mg/L TOC or 300 mg/L COD where influent TOC exceeds 2 g/L with refractory organics and the abatement efficiency is high

    3 · Speciation

    Dissolved CO₂ hydrates slowly to carbonic acid (less than 1 percent of the dissolved gas is H₂CO₃), which dissociates with pKa₁ 6.35 and pKa₂ 10.33 at 25 C when the dissolved gas and the acid are lumped as H₂CO₃*. So below pH 6.3 dissolved CO₂ dominates, between 6.3 and 10.3 bicarbonate, above 10.3 carbonate; nearly all natural water sits in the bicarbonate field, which is why alkalinity and bicarbonate are almost the same number there. In an open system the CO₂ is fixed by Henry's law and the atmosphere; in a closed pipe or aquifer the total inorganic carbon is fixed and pH moves with acid or base added (Stumm and Morgan chapter 4). Organic carbon is not a species but a continuum: dissolved (DOC, through a 0.45 µm filter) and particulate, biodegradable (BOD) and refractory, with the humic fraction that absorbs at 254 nm being the chlorine reactive part.

    conditiondominant speciesnote
    pH below 6.3CO₂ (aq) and H₂CO₃, no carbonate alkalinityacid mine water, soft upland water, soda water, reverse osmosis permeate before remineralisation
    pH 6.3 to 10.3HCO₃⁻all normal natural and treated water; alkalinity equals bicarbonate to within a few percent
    pH above 10.3CO₃²⁻lime softening, lime stabilised sludge, caustic effluent; calcium and magnesium precipitate here
    anoxic sediment, digester, landfillCH₄ with CO₂ and HCO₃⁻the end products of fermentation; digester gas 60 to 70 percent methane (Metcalf and Eddy chapter 10)
    calcite saturationCaCO₃ (s) precipitating or dissolvingthe Langelier index is the pH difference from saturation; positive scales, negative dissolves (MWH chapter 22)
    Solubility
    CO₂ dissolves according to Henry's law, about 10⁻1.5 mol per litre per atmosphere at 25 C, so air equilibrated water holds about 10⁻5 mol/L of CO₂ and rain sits near pH 5.6 (Stumm and Morgan chapter 4). Calcium carbonate is sparingly soluble and its solubility rises with CO₂ partial pressure and falls with temperature, the reason boilers, hot water pipes and reverse osmosis concentrates scale. Methane is a sparingly soluble gas that escapes on aeration.
    Hydrolysis
    Carbonate is a base: it takes a proton from water to give bicarbonate and hydroxide, so soda ash solutions are alkaline; bicarbonate is amphoteric and buffers between pH 6 and 10.
    Complexation
    Carbonate and bicarbonate complex calcium, magnesium and the transition metals (CaCO₃ and MgCO₃ ion pairs, uranyl carbonates that keep uranium mobile) and natural organic matter binds iron, aluminium, copper and lead, slowing their precipitation and passing them through filters (iron chapter); constants not quoted.
    Precipitates
    CaCO₃ (calcite, aragonite) the universal scale; MgCO₃ only in brines, Mg(OH)₂ instead at high pH; FeCO₃ siderite in anoxic groundwater; MnCO₃; the metal carbonates of soda ash precipitation of heavy metals (sodium chapter).
    COX2(g)COX2(aq)\ce{CO2 (g) <=> CO2 (aq)}
    Henry's law, constant about 10^-1.5 mol per litre per atmosphere at 25 C, falling with temperature; the open system boundary condition
    COX2(aq)+HX2OHX2COX3\ce{CO2 (aq) + H2O <=> H2CO3}
    slow hydration, minutes; the ratio H2CO3 to CO2 (aq) is about 10^-3, so the two are lumped as H2CO3* in constants
    HX2COX3HX++HCOX3X\ce{H2CO3 <=> H+ + HCO3^-}
    pKa1 6.35 at 25 C (for H2CO3*), 6.3 to 6.4 across 5 to 25 C; the first buffer point of natural water
    HCOX3XHX++COX3X2\ce{HCO3^- <=> H+ + CO3^2-}
    pKa2 10.33 at 25 C; the second buffer point; carbonate is a minor species below pH 9
    CaCOX3(s)+COX2+HX2OCaX2++2HCOX3X\ce{CaCO3 (s) + CO2 + H2O -> Ca^2+ + 2 HCO3^-}
    dissolution of limestone by carbonic acid, the origin of hardness and alkalinity in most groundwater; runs backwards as scaling when CO2 is lost by heating, aeration or pH rise
    COX3X2+HX2OHCOX3X+OHX\ce{CO3^2- + H2O <=> HCO3^- + OH-}
    hydrolysis of carbonate; soda ash solutions sit near pH 11
    2CX10HX19OX3N+25OX220COX2+16HX2O+2NHX3\ce{2 C10H19O3N + 25 O2 -> 20 CO2 + 16 H2O + 2 NH3}
    complete aerobic oxidation of the Metcalf and Eddy representative wastewater organic C10H19O3N, written with integer coefficients (the text prints half of it); the basis of the ultimate carbonaceous BOD, 1.42 g O2 per g of C5H7NO2 biomass in the same chapter
    CHX3COOHCHX4+COX2\ce{CH3COOH -> CH4 + CO2}
    acetoclastic methanogenesis, the source of about 70 percent of digester methane; the hydrogen route is in the hydrogen chapter (Metcalf and Eddy chapter 10)

    4 · Role in treatment

    as a problem
    disinfection by-product precursors
    natural organic matter, the humic fraction above all, reacts with free chlorine to trihalomethanes and haloacetic acids; formation rises with TOC, chlorine dose, temperature, pH and bromide
    US systems must remove 15 to 50 percent of source TOC by enhanced coagulation or softening according to TOC and alkalinity, unless TOC is below 2 mg/L or SUVA at or below 2.0 L per mg per m (40 CFR 141.135); the by-product limits are in the chlorine chapter
    oxygen demand in receiving water
    biodegradable organic carbon is oxidised by bacteria in the river, which consume dissolved oxygen
    the reason BOD₅ is the oldest effluent parameter: 25 mg/L in the EU, 30 mg/L in the US secondary treatment rule, 30 mg/L in Abu Dhabi marine discharge
    corrosion by aggressive CO₂
    water undersaturated with calcium carbonate dissolves cement, mortar linings and the protective carbonate film on metals
    MWH chapter 22 on the Langelier and calcium carbonate precipitation indices; EU DWD: water should not be aggressive, and demineralised or softened water may need calcium and magnesium salts added
    calcium carbonate scale
    loss of CO₂ or rise of pH or temperature drives bicarbonate to carbonate, which precipitates with calcium
    antiscalant and acid dosing ahead of reverse osmosis; the Langelier index of the concentrate is the design number
    biological regrowth in distribution
    assimilable organic carbon (AOC) and biodegradable DOC feed bacteria in the mains; ozonation raises both by breaking natural organic matter into aldehydes and organic acids
    EPA ozone chapter: oxidation by-products are more biodegradable and are measured as AOC or BDOC; biological filtration after ozone is the control
    activated carbon exhaustion and competition
    natural organic matter occupies the pores meant for micropollutants and chlorine consumes the carbon
    the chlorine chapter has the dechlorination reaction; taste and odour, pesticides and other organics compete on the same surface
    methane in groundwater and digester gas
    dissolved methane strips out in wells and treatment works and forms explosive mixtures
    aeration at the wellhead; digester gas handling; no concentration read
    as a reagent
    carbon dioxide for recarbonation and pH control
    CO₂ converts hydroxide and carbonate back to bicarbonate after lime softening, and lowers pH without mineral acid or added salt; remineralisation of desalinated water with CO₂ and limestone or lime gives calcium and alkalinity
    COX2+COX3X2+HX2O2HCOX3X\ce{CO2 + CO3^2- + H2O -> 2 HCO3^-}
    after lime softening at pH 10 to 11, to about pH 8.5 for a stable water; in remineralisation CO2 dissolves limestone by the calcite equation above (MWH chapter 22)
    granular and powdered activated carbon
    adsorption of dissolved organics in the micropores; capacity described by Freundlich isotherms; GAC in fixed beds after filtration, PAC dosed at the intake for episodic taste and odour; also reduces free chlorine to chloride (chlorine chapter) and supports biological activity as biological activated carbon after ozone
    WHO fact sheets give GAC as the achievable treatment for many organic chemicals (for example 0.001 mg/L for a chlorophenoxy herbicide and 0.1 µg/L for simazine in the fact sheets read); bed life set by natural organic matter, not the target; thermal reactivation
    enhanced coagulation for TOC removal
    aluminium or iron coagulant at depressed pH precipitates natural organic matter with the hydroxide; humic (high SUVA) carbon is removed best
    US Step 2 target pH 5.5 (alkalinity 0 to 60), 6.3 (60 to 120), 7.0 (120 to 240), 7.5 (above 240 mg/L as CaCO3); an extra 10 mg/L alum removing under 0.3 mg/L TOC marks the practical end point
    organic carbon as electron donor for denitrification
    methanol, acetate or the wastewater's own BOD supply the electrons that reduce nitrate to nitrogen gas
    the methanol equation is in the nitrogen chapter
    sodium carbonate and bicarbonate as alkalinity
    soda ash and sodium bicarbonate add alkalinity for nitrification, coagulation and corrosion control without adding hardness
    sodium chapter
    lime softening (carbonate hardness removal)
    lime converts CO₂ and bicarbonate to carbonate, which precipitates with calcium
    Ca(OH)X2+Ca(HCOX3)X22CaCOX3(s)+2HX2O\ce{Ca(OH)2 + Ca(HCO3)2 -> 2 CaCO3 (s) + 2 H2O}
    one mole of lime per mole of calcium bicarbonate, plus one mole for any free CO2 (CO2 + Ca(OH)2 to CaCO3 and water), plus the magnesium demand in the magnesium chapter; pH about 10.3 for calcium alone (MWH chapter 22)
    COX2+Ca(OH)X2CaCOX3(s)+HX2O\ce{CO2 + Ca(OH)2 -> CaCO3 (s) + H2O}
    the first lime demand in softening: free carbon dioxide is neutralised before any hardness is removed

    5 · Removal and control

    biological treatment, aerobic
    activated sludge, biofilm and lagoon bacteria oxidise biodegradable organic carbon to CO₂ and new cells; the sludge is the carbon that did not become CO₂
    2CX10HX19OX3N+25OX220COX2+16HX2O+2NHX3\ce{2 C10H19O3N + 25 O2 -> 20 CO2 + 16 H2O + 2 NH3}
    secondary treatment: BOD5 to 30 mg/L and 85 percent removal (US), 25 mg/L and 70 to 90 percent (EU); the CWW BREF gives BOD5 at or below 20 mg/L as the yearly average from a biological plant
    Efficiency
    85 to 95 percent of BOD₅; COD and TOC less because refractory carbon remains
    Interferences
    toxic loads, low temperature, nutrient deficiency; oxygen transfer is the cost
    anaerobic treatment
    fermentation and methanogenesis convert organic carbon to methane and CO₂ with little sludge and no oxygen; for high strength industrial wastewater and sludge digestion
    CHX3COOHCHX4+COX2\ce{CH3COOH -> CH4 + CO2}
    mesophilic 35 C; methane yield about 0.35 m3 per kg COD removed at standard conditions (Metcalf and Eddy chapter 10)
    Efficiency
    COD removal 70 to 90 percent for suitable wastes; effluent needs aerobic polishing
    Interferences
    sulfate, ammonia, pH below 6.5, temperature
    coagulation for natural organic matter
    precipitation and adsorption of humic substances on aluminium or iron hydroxide at low pH
    US Step 1 TOC removal 15 to 50 percent depending on TOC and alkalinity; softening plants meet the low alkalinity column
    Efficiency
    15 to 50 percent required; humic waters give more, low SUVA waters less
    Interferences
    high alkalinity buffers the pH drop; low SUVA carbon is not amenable and can be waived
    activated carbon adsorption
    GAC beds or PAC dosing take dissolved organics, taste and odour, pesticides and disinfection by-product precursors
    empty bed contact time and carbon use rate from isotherm and column tests (MWH chapter 15)
    Efficiency
    to the µg/L level for target organics while capacity lasts; a fraction of bulk TOC only
    Interferences
    natural organic matter, chlorine, biological growth in the bed
    ozone and biological filtration
    ozone breaks natural organic matter into biodegradable fragments (aldehydes, organic acids) that a biologically active filter then removes as CO₂ and biomass
    EPA ozone chapter: by-products measured as AOC or BDOC; oxygen chapter for the ozone chemistry
    Efficiency
    not quantified in the source
    Interferences
    bromide gives bromate (bromine chapter)
    membrane filtration
    nanofiltration and reverse osmosis reject dissolved organic carbon and bicarbonate; ultrafiltration takes only the particulate and colloidal fraction
    reverse osmosis permeate is CO2 rich and alkalinity poor because CO2 gas passes the membrane while bicarbonate is rejected, hence acidic, aggressive permeate needing remineralisation (general membrane behaviour, MWH chapter 17)
    Efficiency
    DOC rejection high for NF and RO; not quantified here
    Interferences
    organic fouling of the membrane
    inorganic carbon removal
    aeration strips CO₂ and raises pH; acid then degassing converts alkalinity to CO₂ and strips it (decarbonation ahead of demineralisation); lime softening precipitates carbonate as CaCO₃
    HX++HCOX3XCOX2+HX2O\ce{H+ + HCO3^- -> CO2 + H2O}
    acid dosing to pH about 4.5 then a degasser removes the CO2 formed; the last step before mixed bed ion exchange in boiler water treatment (general practice, MWH chapter 16)
    Efficiency
    alkalinity to below 10 mg/L as CaCO₃ with acid and degassing (general)

    6 · Analytics

    methodstandarddetection limitnote
    total and dissolved organic carbon (TOC, DOC)Standard Methods 5310 B (high temperature combustion), C (persulfate UV), D; ISO 8245 and EN 1484; EPA 415.3about 0.1 mg/L in practice (general); not readDOC after 0.45 µm filtration; inorganic carbon purged after acidification or measured and subtracted; the EU allows TOC in place of oxidisability and the UWWTD in place of COD
    chemical oxygen demand (COD)Standard Methods 5220 B, C, D; ISO 6060 (dichromate reflux), ISO 15705 (sealed tube); EPA 410.4about 5 mg/L for the low range (general); not readdichromate in sulfuric acid with silver catalyst and mercury to mask chloride; chloride interferes above the mercury capacity, which is why the CWW BREF prefers TOC (no very toxic reagents)
    biochemical oxygen demand (BOD₅, CBOD₅)Standard Methods 5210 B; ISO 5815-1; EPA 405.1about 2 mg/L (general); not readfive days at 20 C in the dark; a nitrification inhibitor gives CBOD₅ (the UWWTD reference method adds one); seeded dilution water for disinfected effluent
    alkalinityStandard Methods 2320 B; ISO 9963-1 and 9963-2about 1 mg/L as CaCO₃titration with strong acid to pH 4.5 (total) and 8.3 (carbonate); reported as CaCO₃
    free carbon dioxideStandard Methods 4500-CO₂ C (titration) and D (nomograph from pH, alkalinity, temperature and TDS)not applicablemeasure in the field or calculate from pH and alkalinity; CO₂ is lost from the bottle
    UV absorbance and SUVAStandard Methods 5910 Bnot applicableUV₂₅₄ in per metre divided by DOC in mg/L gives SUVA in L per mg per m; 2.0 or below is the US exemption from enhanced coagulation
    adsorbable organic halogen (AOX)ISO 9562not readthe CWW BAT-AEL and ZDHC textile parameter for halogenated organic carbon
    methaneheadspace gas chromatographynot readno standard method read
    Sampling pitfalls
    Fill BOD and TOC bottles without headspace and keep cold; BOD samples must be set up within 48 hours (Standard Methods); TOC bottles must be carbon clean glass with acid preservation for total carbon only where inorganic carbon will be purged. Chlorinated samples need quenching before BOD (and seeding). Alkalinity and CO₂ change with degassing, so titrate promptly or in the field. COD on high chloride samples (seawater, brines) is unreliable; use TOC. Filter for DOC at once, in the field where possible.

    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 guideline for TOC, alkalinity or carbon dioxide; the chlorination by-products (trihalomethanes, haloacetic acids) have guideline values in the chlorine chapter
    EU DWD 2020/2184, total organic carbonnot set Annex I Part C indicator parameter with the parametric value written as no abnormal change; need not be measured for supplies under 10,000 m₃ a day
    EU DWD 2020/2184, oxidisability5.0 mg/L O2Annex I Part C indicator parameter (permanganate index); need not be measured if TOC is analysed
    US EPA, total organic carbonnot set treatment technique, not an MCL: Step 1 TOC removal of 15 to 50 percent by enhanced coagulation or enhanced softening for surface water systems with conventional filtration, by source TOC and alkalinity (40 CFR 141.135); TTHM 0.080 and HAA₅ 0.060 mg/L in the chlorine chapter
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902), TOC10 to 33 mg/Lyearly average, direct discharge to a receiving water; either the TOC or the COD AEL applies, TOC preferred; upper end up to 100 mg/L TOC where influent TOC exceeds 2 g/L with a high proportion of refractory compounds and abatement efficiency is high
    EU CWW BREF BAT-AEL (Decision 2016/902), COD30 to 100 mg/Lyearly average; up to 300 mg/L under the same conditions; no BAT-AEL for BOD, indicative BOD₅ at or below 20 mg/L from a biological plant; TSS 5.0 to 35 mg/L; AOX 0.20 to 1.0 mg/L
    EU UWWTD 2024/3019, Annex I Table 1, secondary treatmentBOD₅ 25; COD 125; TOC 37; TSS 35 mg/L (BOD and COD as O2)
    time-sensitive: recast in force with transposition deadlines
    or minimum reductions of 70 to 90 percent BOD₅, 75 percent COD or TOC, 90 percent TSS; BOD₅ at 20 C without nitrification; the recast repeals Directive 91/271/EEC
    US EPA 40 CFR 133.102, secondary treatmentBOD₅ 30 (30-day average), 45 (7-day average), 85 percent removal; or CBOD₅ 25 and 40 mg/Lwith suspended solids 30 and 45 mg/L and pH 6.0 to 9.0
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)BOD₅ 30; COD 100; TOC 75 mg/L
    region-dependent; marine discharge only
    Table 1 maximum allowable concentrations
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewerCOD 1000 mg/L
    region-dependent; sewer discharge
    Table A₁; no BOD or TOC row for sewer discharge
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), BOD₅textile 30, 15, 8; leather 50, 30, 20 mg/LFoundational, Progressive, Aspirational; Table 3
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), CODtextile 150, 80, 40; leather 250, 150, 100 mg/LFoundational, Progressive, Aspirational; AOX textile only 3, 0.5, 0.1 mg/L

    8 · Health and environmental effects

    Toxicity
    Organic carbon as a bulk parameter is not toxic; its health significance in drinking water is as the precursor of chlorination by-products and as the substrate for regrowth. Carbon dioxide in water is harmless to drink (carbonated bottled water may sit below pH 4.5 under the EU DWD) but the gas is an asphyxiant in confined spaces such as lime softening and CO₂ dosing rooms; methane is an explosion hazard; carbon monoxide is in the element entry.
    Bioaccumulation
    Not applicable to bulk carbon; the persistent halogenated organics counted in AOX include bioaccumulating substances treated under their own entries.
    Ecotoxicity
    Biodegradable organic carbon kills by oxygen depletion, not by toxicity: the reason for BOD limits, the UWWTD and the secondary treatment rule. US EPA has no numeric aquatic criterion for organic carbon; dissolved oxygen is in the oxygen chapter.

    Flags

    • The carbonate constants, Henry's constant and the CaCO₃ equations are cited to Stumm and Morgan chapter 4 from memory of the text, not re-read this session.
    • The municipal wastewater composition is Metcalf and Eddy Table 3-18 from memory of the chapter; the representative organic formula and the methane yield are from chapters 7 and 10 likewise.
    • The TOC and alkalinity bands given as concentrations are the US regulatory bands, not survey data.
    • The UWWTD recast values are read from the 2024 Directive; the 1991 Directive tables (BOD₅ 25 mg/L, COD 125, TSS 35, TN 15 and 10, TP 2 and 1) were not re-read and are not quoted.
    • Detection limits for the organic carbon methods are general laboratory practice, not read.
    • Abu Dhabi values cover two media (marine outfall BOD₅ 30, COD 100, TOC 75 mg/L; sewer COD 1000 mg/L); other GCC states not read.

    Gaps

    • No survey of TOC, DOC or alkalinity in natural waters was read; regulatory bands stand in.
    • No activated carbon isotherm constants, carbon use rates or GAC bed lives are quoted.
    • The WHO GDWQ chapter 10 text on organic carbon, taste and odour and the WHO position on TOC were not read.
    • Chlorination by-product formation kinetics and the trihalomethane formation potential test are not covered here; see the chlorine chapter.
    • The 1991 UWWTD tables, US industrial category BOD and COD limits (OCPSF part 414, textile part 410, pharma part 439) and the EU FDM BREF were not read.
    • Other GCC discharge standards were not read.

    Sources

    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 4 (dissolved carbon dioxide, the carbonate system, alkalinity) and chapter 7 (calcium carbonate solubility)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 2 (BOD, COD, TOC), chapter 3 Table 3-18 (typical composition of untreated wastewater), chapter 7 (stoichiometry of aerobic oxidation) and chapter 10 (anaerobic digestion)
    MWH, Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 15 (adsorption), chapter 16 (ion exchange, decarbonation), chapter 17 (reverse osmosis), chapter 22 (corrosion indices, lime softening, recarbonation)
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Annex I Parts B and C
    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
    Directive (EU) 2024/3019 concerning urban wastewater treatment (recast), Annex I Part B Tables 1 and 2
    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, Alternative Disinfectants and Oxidants Guidance Manual, EPA 815-R-99-014 (April 1999), chapter 3 (ozone by-products, AOC and BDOC)
    WHO GDWQ 4th ed. with addenda (2022), chapter 12 fact sheets read this session (pp. 350, 402, 452, 462, 470): no TOC guideline; GAC as achievable treatment in the organic chemical sheets
    Standard Methods for the Examination of Water and Wastewater (online edition), 2320 alkalinity, 4500-CO2, 5210 BOD, 5220 COD, 5310 TOC, 5910 UV absorbance
    The Element Book, entries for carbon (atmospheric CO2, carbonates, activated charcoal, BOD and COD narrative) (data/elements/C.json, data/reference/text/C.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.