Nitrogen

    group 15 · period 2 · p-block · diatomic nonmetal

    fullNitrogen in water is ammonia, nitrite and nitrate: nitrate and nitrite carry WHO, EU and US drinking water limits for infant methaemoglobinaemia, ammonium is an EU indicator and the parameter that decides whether chlorination gives free chlorine or chloramine, total nitrogen is limited in every European urban and chemical effluent, and nitrification and denitrification are the largest biological processes in wastewater treatment after carbon removal.

    Typical wastewaters

    • municipal sewage urea and protein hydrolysed to ammonia in the sewer; TKN 20 to 70 and ammonia 12 to 45 mg/L as N, nitrate nil in the raw water
    • ammonia and fertiliser manufacture ammonia (NH₃ and NH₄⁺) as N in process wastewater; limits set per 1000 kg of product
    • chemical sector effluent total nitrogen 5 to 25 and inorganic nitrogen 5 to 20 mg/L as N after biological treatment
    • digester supernatant and landfill leachate (sidestreams) warm, ammonia rich liquor, NH₄⁺ at high concentration, treated by anammox, stripping or ion exchange
    • agricultural runoff, manure and septic tank or pit latrine leachate nitrate NO₃⁻ leaching to groundwater from fertiliser and manure, wastewater disposal and the oxidation of nitrogenous waste in excreta
    • textile dyeing and finishing and leather tanning ammonium nitrogen (textile 10, 1, 0.5; leather 15, 10, 1 mg/L as N by level) and total nitrogen
    In the ledger's plant and process records, discharged by: Meat processing (Food and beverage) · Starch production (Food and beverage) · Brewing (Food and beverage) · Dairies (Food and beverage) · Fruit and vegetables (Food and beverage) · Oilseed processing and vegetable oil refining (Food and beverage) · Sugar manufacturing (Food and beverage) · Fish and shellfish processing (Food and beverage) · Grain milling (Food and beverage) · Olive oil processing and refining (Food and beverage) · Wine production (Food and beverage) · Urea and UAN (Chemicals) · NPK and CN fertilisers (Chemicals) · Speciality inorganic explosives (lead azide, lead trinitroresorcinate, lead picrate) (Chemicals) · Speciality inorganic pigments (iron oxide, chromium oxide, CIC, zinc sulphide, lithopone) (Chemicals) · Ammonium nitrate and calcium ammonium nitrate (Chemicals) · Cyanides (sodium and potassium cyanide) (Chemicals) · Ethanolamines (Chemicals) · Nitric acid (Chemicals) · Polyamides (PA 6, PA 66) and their spinning (Chemicals) · Sulphuric acid (Chemicals) · Superphosphates (Chemicals) · Animal feed (Food and beverage) · Cleaning (Food and beverage) · Coffee manufacturing (Food and beverage) · Ethanol production (Food and beverage) · Maize starch (Food and beverage) · Modified (physical/chemical) starches (Food and beverage) · Potato starch (Food and beverage) · Soft drinks and nectar/juice (Food and beverage) · Sweeteners (Food and beverage) · Thawing processes (Food and beverage) · Waste water treatment (Food and beverage) · Wheat starch (Food and beverage) · Yeast (Food and beverage) · Base metal ores (Cu, Ni, Pb, Sn, Zn) (Mining) · Gold leaching with cyanide (Mining) · Heap leach pad (Mining) · Iron ore and other metalliferous ores (Co, Cr, Mn, Mo, V, W) (Mining) · Surface extraction (Mining) · Underground extraction (Mining) · N-acylation (Pharmaceuticals) · Phosgenation (Pharmaceuticals) · Sulphonation (Pharmaceuticals)

    1 · Identity

    Symbol, number
    N, 7
    Oxidation states in water
    -3 as ammonia and ammonium (free ammonia NH₃ and the ammonium ion NH₄⁺, together called ammonia by WHO) and as organic nitrogen in urea, amino acids and proteins (Kjeldahl nitrogen is organic plus ammonia nitrogen); 0 as dissolved N₂, the end product of denitrification and anammox and an inert gas otherwise; +3 as nitrite NO₂⁻, the unstable intermediate of nitrification and denitrification; +5 as nitrate NO₃⁻, the stable oxidised form and the mobile groundwater contaminant. Chloramines (-3 nitrogen bound to +1 chlorine) and nitrogen trichloride are in the chlorine chapter.
    Note
    The element entry carries the Haber process, the fertiliser economy and the eutrophication narrative. This chapter is the nitrogen species in water, their limits and their treatment. Breakpoint chlorination and chloramination are written out in the chlorine chapter and only referenced; struvite is in the magnesium chapter; hydrogen driven denitrification is in the hydrogen chapter.

    2 · Occurrence in water

    Natural sources
    Nitrate is part of the nitrogen cycle and an important plant nutrient; nitrite is not usually present in significant concentrations except under reducing conditions because nitrate is the more stable state (WHO fact sheet). Natural groundwater nitrate does not usually exceed 4 to 9 mg/L as nitrate ion and nitrite 0.3 mg/L; natural vegetation occasionally raises groundwater nitrate; rainwater carries up to 5 mg/L nitrate in industrial areas (WHO background document). Natural ammonia in groundwater and surface water is usually below 0.2 mg/L, up to 3 mg/L in anaerobic groundwater and strata rich in humic substances or iron (WHO ammonia document).
    Anthropogenic sources
    Excess application of inorganic nitrogen fertilisers and manures, wastewater disposal, oxidation of nitrogenous waste in human and animal excreta including septic tanks and pit latrines, and nitrification in source water or distribution systems (WHO); intensive rearing of farm animals gives much higher surface water ammonia; chloramination adds ammonia to drinking water and cement mortar linings release it (WHO ammonia document); ammonia plants and fertiliser works (US effluent guideline part 418), coke ovens, primary beryllium raffinate (299,400 mg/kg as N daily maximum in 40 CFR 421.152), landfill leachate and digester supernatant (Metcalf and Eddy).
    matrixtypical rangenote
    groundwater, natural nitrate4 to 9 mg/L as nitrate ion
    region-dependent; WHO compilation
    usually not exceeded where uncontaminated; up to 1500 mg/L found in an agricultural area of India; rising 0.2 to 1.3 mg/L per year in parts of Denmark and the Netherlands; US: most supplies below 4 mg/L, above 20 mg/L in about 6 percent of groundwaters and 3 percent of surface waters
    surface water, nitrate0 to 18 mg/L as nitrate ion
    region-dependent; old compilation
    normally low (up to about 4 mg/L as nitrate nitrogen); drinking water from surface water in most countries below 10 mg/L; 0.5 to 10 percent of supplies above 50 mg/L in 15 European countries (1985)
    groundwater and surface water, nitritemedian 0.07 (groundwater) and 0.1 (surface water) mg/L as nitrite ionUS surveyUS survey; normally below a few mg/L; in distribution systems that chloraminate, nitrification can add 0.2 to 1.5 mg/L and occasionally more than 3 mg/L
    groundwater and surface water, ammoniabelow 0.2 mg/Lnatural levels; anaerobic groundwater up to 3 mg/L; surface water up to 12 mg/L where animals are reared intensively
    seawater, nitrogen0.5 mg/Lsingle figureoceanic abundance figure for the element, Jefferson Lab via PubChem, quoted in the element entry; mostly dissolved N₂ with nitrate in deep water
    untreated municipal wastewaterTKN 20 to 70; ammonia 12 to 45; nitrate 0 mg/L as Ntextbook typical valueslow to high strength typical composition, Metcalf and Eddy Table 3-18, from the chapter and not re-read; nitrogen enters as urea and protein and is hydrolysed to ammonia in the sewer
    industrial wastewater, chemical sector after treatmentTN 5 to 25; inorganic N 5 to 20 mg/L as N
    achievable levels, not raw effluent
    CWW BAT-AEL yearly averages; up to 40 and 35 mg/L where the abatement efficiency is at least 70 percent; the AELs do not apply to installations without biological treatment

    3 · Speciation

    Ammonia dissolves to give ammonium and hydroxide with a base constant of 1.78 x 10⁻5 (WHO), that is pKa 9.25 for NH₄⁺ at 25 C: below pH 8 nearly all ammonia is the ionised, non volatile, non toxic NH₄⁺, at pH 9.25 half is the free NH₃ that is toxic to fish, volatile and the species that stripping towers remove; the fraction rises with temperature. Nitrate and nitrite are fully dissociated anions at every pH, do not adsorb, do not precipitate and are removed only by membranes, resins or bacteria. Redox, not pH, moves nitrogen between the three: oxic water with nitrifiers turns ammonia to nitrite and nitrate within days, anoxic water with organic carbon turns nitrate back to nitrogen gas, and nitrite accumulates wherever either process is incomplete, in chloraminated mains, galvanised pipes with stagnant water, and overloaded nitrifying filters (WHO).

    conditiondominant speciesnote
    oxic water, pH 6 to 8, nitrifying bacteria presentNO₃⁻ (stable end product); NH₄⁺ only transientlyrivers, oxic aquifers, nitrified effluent
    anoxic water, organic carbon presentNH₄⁺ from ammonification; nitrate denitrified to N₂anaerobic groundwater with up to 3 mg/L ammonia; anoxic zones of activated sludge plants
    pH above 9.25NH₃ (free ammonia) dominantammonia stripping at pH 10.5 to 11.5; free ammonia toxicity in alkaline lagoons
    chloraminated distribution waterNH₂Cl with free NH₃, and NO₂⁻ where nitrifiers coloniseWHO: nitrite occurrence under chloramination is almost invariably intermittent; monitor disinfectant residual, microbiology and nitrite
    chlorinated water, Cl₂ to N above 7.6 to 1N₂, NO₃⁻ and NCl₃ past the breakpointchlorine chapter
    Solubility
    Ammonia gas is very soluble, 421 g/L at 20 C (WHO); all ammonium, nitrite and nitrate salts of the common cations are soluble, so none of the three has a solubility control in water; nitrogen gas is sparingly soluble and supersaturates in denitrifying clarifiers, floating sludge.
    Hydrolysis
    Ammonium is a weak acid (pKa 9.25), ammonia a weak base; nitrate and nitrite are the anions of strong and moderately weak acids (nitrous acid pKa about 3.3) and are not hydrolysed at natural pH. Urea hydrolyses to ammonia and CO₂ in the sewer and in the soil.
    Complexation
    Ammonia complexes copper, nickel, silver and zinc as ammines in plating rinses and in chloraminated water, keeping them dissolved; nitrate complexes weakly and nitrite forms nitroso complexes with iron; none quantified here.
    Precipitates
    None of the three species alone. Magnesium ammonium phosphate (struvite) precipitates from digester liquors and can be made deliberately (magnesium chapter); ammonium ion exchanges onto clinoptilolite.
    NHX3+HX2ONHX4X++OHX\ce{NH3 + H2O <=> NH4^+ + OH-}
    base constant 1.78 x 10^-5 (WHO ammonia document); the degree of ionisation depends on temperature, pH and dissolved salts
    NHX4X+NHX3+HX+\ce{NH4^+ <=> NH3 + H+}
    pKa 9.25 at 25 C; the acid form of the same equilibrium, used for the un-ionised ammonia fraction in toxicity criteria (Metcalf and Eddy chapter 2)
    CO(NHX2)X2+HX2O2NHX3+COX2\ce{CO(NH2)2 + H2O -> 2 NH3 + CO2}
    urease hydrolysis of urea in sewers and soil; the reason raw sewage nitrogen arrives as ammonia
    2NHX4X++3OX22NOX2X+4HX++2HX2O\ce{2 NH4^+ + 3 O2 -> 2 NO2^- + 4 H+ + 2 H2O}
    first nitrification step, ammonia oxidising bacteria and archaea; the acid produced consumes alkalinity
    2NOX2X+OX22NOX3X\ce{2 NO2^- + O2 -> 2 NO3^-}
    second nitrification step, nitrite oxidising bacteria; slower to start after cold or toxic shock, so nitrite appears
    NHX4X++2OX2NOX3X+2HX++HX2O\ce{NH4^+ + 2 O2 -> NO3^- + 2 H+ + H2O}
    overall nitrification; 4.57 g O2 per g of ammonia nitrogen oxidised (4.33 g when cell synthesis is included) and 7.14 g of alkalinity as CaCO3 consumed per g of nitrogen (Metcalf and Eddy chapter 7); optimum pH 7.5 to 8, slow below 10 C, washout at short sludge ages
    6NOX3X+5CHX3OH3NX2+5COX2+7HX2O+6OHX\ce{6 NO3^- + 5 CH3OH -> 3 N2 + 5 CO2 + 7 H2O + 6 OH-}
    heterotrophic denitrification with methanol, anoxic; 2.47 g methanol per g of nitrate nitrogen and 3.57 g alkalinity as CaCO3 returned per g of nitrogen (Metcalf and Eddy chapter 7); wastewater BOD, acetate or hydrogen serve as well
    NHX4X++NOX2XNX2+2HX2O\ce{NH4^+ + NO2^- -> N2 + 2 H2O}
    anaerobic ammonium oxidation (anammox), anoxic, on sidestreams such as digester dewatering liquor after partial nitritation; saves about 60 percent of the oxygen and all the carbon of the conventional route (Metcalf and Eddy chapter 15)
    2NHX3+3HOClNX2+3HX++3ClX+3HX2O\ce{2 NH3 + 3 HOCl -> N2 + 3 H+ + 3 Cl^- + 3 H2O}
    breakpoint chlorination, Cl2 to N 7.6 to 1 by weight; the chloramine steps and the ratio are in the chlorine chapter

    4 · Role in treatment

    as a problem
    nitrate in groundwater supplies
    stable, highly soluble, low potential for co-precipitation and adsorption; conventional coagulation, sedimentation, filtration and chlorination do not remove it
    WHO: prevention (fertiliser and manure management, siting of latrines and septic tanks) and blending first; treatment by ion exchange, reverse osmosis, electrodialysis or biological denitrification, all with cost, complexity and resin, brine or reject disposal
    ammonia and chlorination
    ammonia consumes chlorine as chloramine before any free residual forms; up to 68 percent of the chlorine can react with ammonia; taste and odour appear when water above 0.2 mg/L ammonia is chlorinated
    WHO ammonia document; the breakpoint arithmetic is in the chlorine chapter
    nitrite in distribution
    nitrification of free ammonia (natural or from chloramination) by bacteria in the mains, in stagnant nitrate rich water in galvanised steel pipes, and on filters colonised by ammonium oxidisers
    WHO: nitrite formation is the reason for the EU 0.10 mg/L ex works value and the requirement to monitor ammonium and nitrite where chloramination is used (DWD Annex II)
    manganese filter failure
    elevated ammonia consumes the oxygen on manganese removal filters through nitrification, giving mouldy, earthy tasting water
    WHO ammonia document
    infant methaemoglobinaemia
    nitrite, formed from nitrate by gut bacteria, oxidises haemoglobin; bottle fed infants under 3 months with gastrointestinal infection are the cases, almost all from private wells
    97 percent of cases above 44.3 mg/L nitrate (WHO); boil only to a rolling boil because boiling concentrates nitrate
    eutrophication and oxygen demand
    nitrogen with phosphorus feeds algal growth; nitrification of effluent ammonia consumes 4.57 g oxygen per g N in the river
    the reason for TN limits (UWWTD 10 and 8 mg/L, CWW 5 to 25 mg/L) and ammonia limits (Abu Dhabi marine 2.0 mg/L as N)
    un-ionised ammonia toxicity to fish
    NH₃, not NH₄⁺, crosses gills; the fraction rises with pH and temperature
    US criteria are pH and temperature dependent: 17 mg total ammonia nitrogen per litre acute and 1.9 mg/L chronic at pH 7 and 20 C
    alkalinity loss in nitrifying plants
    7.14 g alkalinity as CaCO₃ consumed per g N nitrified; pH falls and nitrification stops in soft water
    lime, caustic or sodium bicarbonate dosing, or denitrification to return 3.57 g per g N (Metcalf and Eddy)
    nitrogen gas in clarifiers
    denitrification in the sludge blanket floats sludge
    Metcalf and Eddy; the cure is an anoxic zone upstream
    as a reagent
    ammonia for chloramination
    ammonia or ammonium sulfate dosed with chlorine at Cl₂ to N 3 to 1 to 5 to 1 by weight to form monochloramine, a persistent secondary disinfectant
    NHX3+HOClNHX2Cl+HX2O\ce{NH3 + HOCl -> NH2Cl + H2O}
    chlorine chapter; the free ammonia left over feeds nitrifiers, which is the nitrite problem above
    nitrogen nutrient dosing
    industrial wastewaters short of nitrogen (food, pulp, petrochemical) need ammonia or urea for biological treatment
    about 5 parts nitrogen per 100 parts BOD5 (BOD to N to P about 100 to 5 to 1) is the working ratio (Metcalf and Eddy chapter 7)
    nitrate as an electron acceptor for odour control
    calcium or sodium nitrate dosed to sewers and sludge holding tanks keeps the redox above sulfate reduction, preventing hydrogen sulfide
    sulfur chapter for the sulfide chemistry; general practice named in Metcalf and Eddy chapter 6
    ammonia to suppress bromate
    ammonia added with short ozone contact time decreases bromate and brominated organics
    EPA ozone chapter

    5 · Removal and control

    biological nitrification and denitrification
    aerobic nitrification of ammonia to nitrate at a sludge age long enough for the slow growing autotrophs, then anoxic denitrification to nitrogen gas with wastewater carbon (pre-anoxic, with internal recycle) or added methanol (post-anoxic)
    NHX4X++2OX2NOX3X+2HX++HX2O\ce{NH4^+ + 2 O2 -> NO3^- + 2 H+ + H2O}
    sludge age above about 10 days at 10 C for nitrification; dissolved oxygen above 2 mg/L in the aerobic zone and below 0.2 in the anoxic zone; alkalinity 7.14 g per g N consumed, 3.57 g per g N returned (Metcalf and Eddy chapters 7 and 8)
    Efficiency
    effluent ammonia below 1 mg/L as N; total nitrogen 5 to 10 mg/L as N in a well designed plant; 80 percent reduction is the UWWTD requirement
    Interferences
    cold, low alkalinity, toxic shock, low carbon to nitrogen ratio for denitrification
    anammox sidestream treatment
    partial nitritation of about half the ammonia followed by anaerobic ammonium oxidation with that nitrite
    NHX4X++NOX2XNX2+2HX2O\ce{NH4^+ + NO2^- -> N2 + 2 H2O}
    warm, ammonia rich digester liquor (Metcalf and Eddy chapter 15); slow growing biomass held as granules or on carriers
    Efficiency
    about 80 to 90 percent of sidestream nitrogen (general figure, not from the source)
    Interferences
    nitrite oxidisers taking the nitrite to nitrate; low temperature
    ion exchange for nitrate
    strong base anion resin in chloride form takes nitrate; nitrate selective resins reduce sulfate competition; regenerated with brine
    NOX3X+RClRNOX3+ClX\ce{NO3^- + RCl -> RNO3 + Cl^-}
    R is the resin; US BAT 5 for nitrate and nitrite; WHO lists it among the effective central technologies with over 80 percent removal to as low as 13 mg/L
    Efficiency
    over 80 percent (WHO)
    Interferences
    sulfate competes and causes nitrate dumping on a conventional resin when the bed is exhausted; brine disposal
    reverse osmosis and electrodialysis
    membrane rejection of the nitrate anion; electrodialysis moves it through anion membranes
    US BAT 7 and 9 for nitrate; WHO: capable of removing over 80 percent
    Efficiency
    over 80 percent (WHO)
    Interferences
    reject water disposal; nitrate rejection by RO is lower than for divalent ions (general)
    biological denitrification of drinking water
    heterotrophic bacteria on a fixed bed with added carbon (ethanol, acetate) or autotrophs with hydrogen or sulfur reduce nitrate to N₂; followed by aeration and filtration
    6NOX3X+5CHX3OH3NX2+5COX2+7HX2O+6OHX\ce{6 NO3^- + 5 CH3OH -> 3 N2 + 5 CO2 + 7 H2O + 6 OH-}
    WHO lists biological denitrification among the effective methods; the hydrogen route is in the hydrogen chapter
    Efficiency
    over 80 percent (WHO)
    Interferences
    carbon carry over, nitrite breakthrough, biological stability of the product
    ammonia stripping
    lime raises pH to 10.5 to 11.5, converting ammonium to free ammonia, which a countercurrent air tower strips; the air is scrubbed with acid to recover ammonium sulfate
    NHX4X++OHXNHX3(g)+HX2O\ce{NH4^+ + OH- -> NH3 (g) + H2O}
    sidestreams and industrial ammonia liquors; calcium carbonate scaling of the packing and poor cold weather performance (Metcalf and Eddy chapter 15)
    Efficiency
    90 percent and above at high pH and air to water ratio (general, not from the source)
    Interferences
    scaling, temperature
    ion exchange for ammonium
    clinoptilolite, a natural zeolite selective for ammonium over calcium and magnesium; regenerated with brine or lime
    NHX4X++NaRNHX4R+NaX+\ce{NH4^+ + NaR -> NH4R + Na^+}
    R is the zeolite; Metcalf and Eddy chapter 15; small flows and tertiary polishing
    Efficiency
    not quantified in the source
    Interferences
    suspended solids, competing cations
    breakpoint chlorination
    chlorine oxidises ammonia to nitrogen gas at Cl₂ to N 7.6 to 1
    chlorine chapter; used for polishing low ammonia concentrations, not for loads, because of the chlorine demand and the chloride and by-products left
    Efficiency
    to below detection
    Interferences
    organic nitrogen forms organic chloramines
    nitrite oxidation
    any disinfectant oxidises nitrite to nitrate
    WHO: treatment focuses on nitrate because nitrite is readily converted by many disinfectants
    Efficiency
    complete
    Interferences
    consumes disinfectant
    struvite precipitation
    ammonium removed with phosphate and magnesium as a fertiliser product
    magnesium chapter; limited by phosphate, not ammonium, so it removes a minor share of sidestream nitrogen
    Efficiency
    nitrogen removal small

    6 · Analytics

    methodstandarddetection limitnote
    ammonia by indophenol (phenate) colorimetryStandard Methods 4500-NH₃ F and G; ISO 7150-1 and ISO 11732 (flow analysis); EPA 350.10.025 to 3 mg/L working range (WHO)the ZDHC methods; distillation (4500-NH₃ B) for coloured or turbid samples
    ammonia selective electrodeStandard Methods 4500-NH₃ D and E; EPA 350.3not readsample made alkaline so all ammonia is NH₃; fast for wastewater
    nitrate and nitrite by ion chromatographyEPA 300.0 and 300.1; Standard Methods 4110 B; ISO 10304-1MDL 0.009 mg/L as nitrate ion and 0.013 mg/L as nitrite ion (WHO)the reference method at guideline levels
    nitrate by cadmium reduction colorimetryStandard Methods 4500-NO₃ E and F; EPA 353.2MDL 0.04 to 4.4 mg/L as nitrate ion (WHO)recommended by WHO for nitrate below 0.4 mg/L; nitrite by diazotisation (4500-NO₂ B) measured with and without reduction
    nitrate by UV absorbanceStandard Methods 4500-NO₃ Bnot readscreening only; organic matter interferes
    Kjeldahl and total nitrogenStandard Methods 4500-Norg B and C (Kjeldahl), 4500-N B and C (persulfate digestion); ISO 11905-1; ISO 29441; EPA 351.2not readTKN is organic plus ammonia nitrogen; total nitrogen adds nitrite and nitrate; the ZDHC and UWWTD parameter
    Sampling pitfalls
    Nitrogen species change in the bottle: ammonia is nitrified and nitrite oxidised in oxic samples, nitrate is denitrified in anoxic ones. Cool to 4 C and analyse within 48 hours, or acidify to pH below 2 with sulfuric acid for ammonia, Kjeldahl and nitrate plus nitrite together (acid destroys nitrite as a separate species). Quench chlorine or chloramine before ammonia analysis, and remember that monochloramine reads as ammonia after dechlorination. Report the units: nitrate as NO₃ (WHO, EU) is 4.43 times nitrate as N (US); nitrite as NO₂ is 3.29 times nitrite as N (WHO conversion factors 0.226 and 0.304).

    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), nitrate50 mg/L as nitrate ionprotective against methaemoglobinaemia and thyroid effects in bottle fed infants; equals 11.3 mg/L as nitrate nitrogen; assessment 2016
    WHO GDWQ, nitrite3 mg/L as nitrite ionderived from the 50 mg/L nitrate value, its molar equivalent as nitrite, a 0.1 conversion factor and 100 percent allocation to water for infants under 6 months; the sum of the ratios of nitrate and nitrite to their guideline values should not exceed 1; the former long term nitrite value is gone
    WHO GDWQ, ammoniano guideline occurs at concentrations well below health concern (toxic effects only above about 200 mg/kg body weight); odour threshold about 1.5 mg/L and taste threshold 35 mg/L for ammonium; compromises disinfection, forms nitrite in distribution, fails manganese filters
    EU DWD 2020/2184, nitrate50 mg/LAnnex I Part B; the condition nitrate over 50 plus nitrite over 3 not exceeding 1 must be met
    EU DWD 2020/2184, nitrite0.50 mg/LAnnex I Part B; 0.10 mg/L ex water treatment works; the same combined condition
    EU DWD 2020/2184, ammonium0.50 mg/LAnnex I Part C indicator parameter; ammonium and nitrite join the Group A monitoring list where chloramination is used
    US EPA NPDWR, nitrate10 mg/L as NMCL and MCLG; equals 44.3 mg/L as nitrate ion; BAT ion exchange, reverse osmosis, electrodialysis
    US EPA NPDWR, nitrite1 mg/L as NMCL and MCLG; total nitrate plus nitrite 10 mg/L as N; BAT ion exchange, reverse osmosis
    US EPA, ammonianot regulated no primary or secondary standard; chloramine residual limited at 4.0 mg/L as Cl₂ (chlorine chapter)
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902), total nitrogen5.0 to 25 mg/L as Nyearly average; or total inorganic nitrogen 5.0 to 20 mg/L; upper ends up to 40 and 35 mg/L where abatement efficiency is at least 70 percent; not applicable without biological treatment; the lower end is reached with low influent nitrogen or optimised nitrification and denitrification
    EU UWWTD 2024/3019, Annex I Table 2, tertiary treatment10 (10,000 to below 150,000 p.e.); 8 (150,000 p.e. and above) mg/L as N
    time-sensitive: recast with staged deadlines
    total nitrogen, or 80 percent minimum reduction; total phosphorus 0.7 and 0.5 mg/L
    US EPA 40 CFR 418.22 and 418.23, fertiliser manufacturing, ammonia subcategoryBPT 0.1875 daily maximum, 0.0625 30-day average; BAT 0.05 and 0.025 kg ammonia as N per 1000 kg of productproduction normalised unitsproduction based; pH 6.0 to 9.0
    US EPA 40 CFR 133.102, secondary treatmentnot set no federal nitrogen limit in the secondary treatment rule; nitrogen limits are permit specific water quality based limits derived from the ammonia criteria
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)ammonia 2.0; nitrate 30.0; TKN 10 mg/L as N
    region-dependent; marine discharge only
    Table 1
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewerTKN 150 mg/L
    region-dependent; sewer discharge
    Table A₂; no ammonia or nitrate row
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), ammonium nitrogentextile 10, 1, 0.5; leather 15, 10, 1 mg/L as NFoundational, Progressive, Aspirational; phenate or ammonia electrode methods only
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), total nitrogentextile 20, 10, 5; leather 35, 20, 10 mg/L as NFoundational, Progressive, Aspirational
    irrigationFAO Irrigation and Drainage Paper 29 (1985), Table 1, nitrate nitrogenbelow 5 no restriction; 5 to 30 slight to moderate; above 30 severe mg/L as Naffects susceptible crops (lodging, delayed ripening); ammonium and organic nitrogen are included when wastewater is tested

    8 · Health and environmental effects

    Toxicity
    Nitrate is absorbed over 90 percent and about 25 percent is recirculated in saliva, where mouth bacteria convert about 20 percent to nitrite; the body itself makes about 62 mg nitrate a day. Nitrite oxidises haemoglobin to methaemoglobin, and above 10 percent methaemoglobin infants turn blue; 97 percent of clinical cases were above 44.3 mg/L nitrate and almost all under 3 months old with gastrointestinal infection. Nitrate competitively inhibits iodide uptake with weak evidence of thyroid effects above 50 mg/L. IARC: ingested nitrate or nitrite under conditions of endogenous nitrosation is probably carcinogenic (Group 2A), nitrate alone is not; the weight of evidence does not support an association between drinking water nitrate and cancer (WHO). Ammonia is a key metabolite made at 4000 mg/day in the intestine; environmental exposure is insignificant beside it (WHO ammonia document).
    Bioaccumulation
    Not applicable; nitrogen is cycled, not accumulated.
    Ecotoxicity
    US EPA 2013 freshwater ammonia criteria: 17 mg total ammonia nitrogen per litre acute and 1.9 mg/L chronic (30-day average, 4-day average not above 4.8 mg/L) at pH 7 and 20 C, falling steeply as pH and temperature rise because the toxic species is NH₃; based on sensitive freshwater mussels and snails. Nitrate and nitrite have no US aquatic criterion in the table read; nitrite is toxic to fish (brown blood disease) at mg/L levels (general, not from a source read). Nitrogen with phosphorus drives eutrophication, the reason for the UWWTD nutrient limits.

    Flags

    • Nitrification and denitrification stoichiometry, oxygen and alkalinity factors, pKa 9.25 and the wastewater composition are cited to Metcalf and Eddy chapters 2, 3, 7, 8 and 15 from memory of the text, not re-read this session.
    • The anammox and stripping efficiencies are general figures, not from the sources read.
    • WHO occurrence data are compilations of 1980s to 2010s surveys and vary strongly by region.
    • The US ammonia effluent guideline values are production normalised, not concentrations.
    • The UWWTD figures are from the 2024 recast; the 1991 Directive values (15 and 10 mg/L TN) were not re-read.
    • Abu Dhabi values cover two media (marine outfall ammonia 2.0, nitrate 30, TKN 10 mg/L as N; sewer TKN 150 mg/L); other GCC states not read.

    Gaps

    • No survey of nitrogen in industrial effluents beyond the CWW AELs was read; fertiliser, coke oven and landfill leachate concentrations belong to the ledger.
    • No ion exchange capacities, membrane rejections or denitrification filter loading rates are quoted.
    • Nitrous oxide emissions from nitrification and denitrification, and organic nitrogen compounds (nitrosamines, which are in the WHO fact sheets), are not covered here.
    • The pH and temperature dependence of the US ammonia criteria is not tabulated; only the pH 7, 20 C values are quoted.
    • The 1991 UWWTD table and the US industrial category nitrogen limits other than part 418 and 421 were not read.
    • Other GCC discharge standards were not read.

    Sources

    WHO Guidelines for Drinking-water Quality, 4th ed. incorporating the first and second addenda (2022), chapter 12 chemical fact sheet, Nitrate and nitrite (pp. 438 to 444)
    WHO, Nitrate and Nitrite in Drinking-water, background document for development of WHO Guidelines for Drinking-water Quality, WHO/FWC/WSH/16.52 (2016), sections 1 and 2 (environmental levels)
    WHO GDWQ 4th ed. with addenda (2022), chapter 12 chemical fact sheet, Ammonia (pp. 335 to 336)
    WHO, Ammonia in Drinking-water, background document, WHO/SDE/WSH/03.04/01 (2003; text of 1996)
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Annex I Parts B and C
    US EPA, National Primary Drinking Water Regulations (table of MCLs and MCLGs)
    40 CFR 141.62, Maximum contaminant levels for inorganic contaminants, with the BAT table and key
    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)
    40 CFR 418.22 (BPT) and 418.23 (BAT), Ammonia subcategory, fertilizer manufacturing point source category
    Abu Dhabi Specification ADS 23/2017, Environmental Specifications for Land-Based Liquid Discharges to the Marine Environment (Environment Agency Abu Dhabi), Table 1
    Abu Dhabi Department of Energy, Trade Effluent Control Regulations 2022 (DoE/PD/R01/005, effective 1 January 2022), Schedule A Tables A1, A2 and A4
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), Table 3 conventional parameters and anions
    Ayers, R. S. and Westcot, D. W., Water Quality for Agriculture, FAO Irrigation and Drainage Paper 29 Rev. 1 (1985), Table 1
    US EPA, Aquatic Life Ambient Water Quality Criteria for Ammonia, Freshwater 2013, EPA 822-R-13-001 (executive summary and criteria table)
    US EPA, National Recommended Water Quality Criteria, Aquatic Life Criteria Table
    US EPA, Alternative Disinfectants and Oxidants Guidance Manual, EPA 815-R-99-014 (April 1999), chapter 3 (ammonia and bromate) and chapter 6 (chloramines, breakpoint, Table 6-1)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 2 (nitrogen forms, ammonia equilibrium), chapter 3 Table 3-18, chapter 7 (nitrification and denitrification stoichiometry), chapter 8 (process design), chapter 15 (anammox, stripping, ion exchange)
    Standard Methods for the Examination of Water and Wastewater (online edition), 4500-NH3, 4500-NO2, 4500-NO3, 4500-Norg, 4500-N, 4110
    The Element Book, entries for nitrogen (seawater abundance, fertiliser economy, eutrophication narrative) (data/elements/N.json, data/reference/text/N.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.