Phosphorus

    group 15 · period 3 · p-block · polyatomic nonmetal

    fullPhosphorus has no drinking water limit but is the nutrient that every wastewater discharge consent in Europe now regulates to 0.5 to 2 mg/L, the target of chemical and biological phosphorus removal, the recoverable resource in struvite, and, as phosphate and phosphonate, the sequestrant and antiscalant chemistry of membranes and mains.

    Typical wastewaters

    • municipal sewage orthophosphate, polyphosphate and organic phosphorus from excreta and detergents; total phosphorus 4 to 12 mg/L as P
    • digester liquor and sludge dewatering sidestreams orthophosphate released in anaerobic digestion with ammonium and magnesium, crystallising as struvite at pH 8.5 to 9
    • chemical sector effluent (cooling and heating systems, nutrient dosing) orthophosphate, polyphosphate and phosphonate from cooling and boiler conditioning and phosphate added as nutrient for the biological plant; total phosphorus 0.50 to 3.0 mg/L
    • textile dyeing and finishing total phosphorus 0.4 to 2 mg/L BAT-AEL for direct discharge
    • reverse osmosis concentrate phosphonate antiscalant (an HEDP derivative dosed at 5 mg/L in the case read) concentrated in the reject, counted as total phosphorus
    In the ledger's plant and process records, discharged by: Cleaning-in-place and disinfection (Food and beverage) · Phosphorus compounds (PCl3, POCl3, PCl5) (Chemicals) · Brewing (Food and beverage) · Fruit and vegetables (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) · Starch production (Food and beverage) · Sugar manufacturing (Food and beverage) · Wine production (Food and beverage) · Phosphoric acid (wet process) (Chemicals) · Polystyrene (GPPS, HIPS, EPS) (Chemicals) · Cleaning (Food and beverage) · Meat processing (Food and beverage) · Thawing processes (Food and beverage)

    1 · Identity

    Symbol, number
    P, 15
    Oxidation states in water
    +5 only in practice: orthophosphate (H₃PO₄, H₂PO₄⁻, HPO₄²⁻, PO₄³⁻), condensed polyphosphates that hydrolyse back to orthophosphate, organic phosphorus esters, and phosphonates (C-P bonded antiscalants such as HEDP and ATMP). Analysts split total phosphorus into reactive (ortho), acid hydrolysable (poly) and organic fractions.
    Note
    The element entry covers phosphate rock, phosphoric acid and the eutrophication warning. This chapter is the wastewater engineer's phosphorus: speciation by pH, metal salt and lime precipitation, enhanced biological removal, struvite and the limits that drive them.

    2 · Occurrence in water

    Natural sources
    Weathering of apatite gives low natural orthophosphate; most surface water phosphorus is bound to particles and to iron oxides and is released from sediments under anoxic conditions. Phosphate is the limiting nutrient of most fresh waters (the element entry).
    Anthropogenic sources
    Sewage (excreta, detergents where not banned), agricultural runoff and manure, phosphate fertiliser and phosphoric acid plants, food and dairy processing, cooling water and boiler conditioning with phosphates and phosphonates (the CWW BAT conclusions note phosphorus originating from heating or cooling systems), and phosphorus added deliberately to industrial biological treatment as a nutrient.
    matrixtypical rangenote
    untreated municipal wastewater4 to 12 mg/L as P
    textbook typical values, region-dependent
    total phosphorus, weak to strong domestic wastewater (Metcalf and Eddy chapter 3 typical composition table, from the chapter, not re-read)
    seawater0.06 mg/L
    single figure; surface ocean is nutrient depleted
    estimated oceanic abundance, Jefferson Lab figure via PubChem, as in the element entry

    3 · Speciation

    Orthophosphate is a triprotic acid with pKa values near 2.1, 7.2 and 12.3, so in natural and waste water it is a mixture of H₂PO₄⁻ and HPO₄²⁻ around neutral pH, shifting to HPO₄²⁻ above pH 7.2; the fully deprotonated PO₄³⁻ only matters at the high pH of lime treatment. Polyphosphates hydrolyse slowly to orthophosphate, faster when warm and acidic; organic phosphorus is released by biological oxidation. Metal cations precipitate orthophosphate: aluminium and iron(III) as AlPO₄ and FePO₄ near neutral pH, calcium as hydroxyapatite above pH 10, magnesium with ammonium as struvite at pH 8.5 to 9. Phosphonates and polyphosphates at a few mg/L hold calcium carbonate and sulfate below their scaling point by threshold inhibition.

    conditiondominant speciesnote
    natural and waste water, pH 6 to 8H₂PO₄⁻ and HPO₄²⁻ (soluble reactive phosphorus); particulate and organic P; polyphosphate from detergents and conditioningthe fraction the ascorbic acid test sees is orthophosphate
    chemical precipitation with Al or Fe(III), pH 5.5 to 7AlPO₄ (s), FePO₄ (s), phosphate adsorbed on Al(OH)₃ and Fe(OH)₃the working range of alum and ferric chloride for phosphorus
    lime treatment, pH above 10hydroxyapatite Ca₅(PO₄)₃OH (s) with CaCO₃ and Mg(OH)₂lime dose is set by alkalinity, not by phosphorus
    anaerobic digester liquor and sludge dewatering, pH 7.5 to 9, high NH₄⁺ and Mg²⁺struvite MgNH₄PO₄.6H₂O (s)a scale in pipes and a product in recovery reactors
    EBPR biomassintracellular polyphosphate, 4 to 15 percent of dry biomass in phosphorus accumulating organisms against about 2 percent in ordinary bacteriathe phosphorus leaves the plant in the waste sludge
    Solubility
    AlPO₄ and FePO₄ have solubility minima near pH 6 to 7 and hydroxyapatite is very insoluble above pH 10; struvite solubility falls with rising pH to a minimum near pH 9 (Wu et al.). Constants are not quoted because the sources read do not print them.
    Hydrolysis
    Polyphosphates (tripolyphosphate, hexametaphosphate) hydrolyse to orthophosphate over hours to days, which is why sequestered iron and manganese eventually precipitate and why total phosphorus samples are digested before analysis.
    Complexation
    Phosphate sorbs on iron and aluminium hydroxides and competes with arsenate on adsorbents (EPA arsenic manual, via the arsenic chapter: each 0.5 mg/L of phosphate above 0.2 mg/L cuts granular ferric hydroxide capacity about 30 percent); phosphonates chelate calcium and magnesium and poison crystal growth.
    Precipitates
    AlPO₄, FePO₄, hydroxyapatite Ca₅(PO₄)₃OH and other calcium phosphates, struvite MgNH₄PO₄.6H₂O, vivianite Fe₃(PO₄)₂ in iron dosed anaerobic sludge.
    HX2POX4XHPOX4X2+HX+\ce{H2PO4^- <=> HPO4^2- + H+}
    pKa2 about 7.2 at 25 C; the dissociation that sets the charge of phosphate in treatment (Stumm and Morgan chapter 3, from the chapter, not re-read)
    AlX3++HPOX4X2AlPOX4(s)+HX+\ce{Al^3+ + HPO4^2- -> AlPO4 (s) + H+}
    alum dosing at pH 5.5 to 7; theoretical 1 mol Al per mol P, 1.5 to 3 times that in practice because Al(OH)3 forms in parallel (Metcalf and Eddy chapter 6)
    FeX3++HPOX4X2FePOX4(s)+HX+\ce{Fe^3+ + HPO4^2- -> FePO4 (s) + H+}
    ferric chloride or sulfate dosing at pH 5 to 7; same excess over stoichiometry as aluminium
    5CaX2++3POX4X3+OHXCaX5(POX4)X3OH(s)\ce{5 Ca^2+ + 3 PO4^3- + OH- -> Ca5(PO4)3OH (s)}
    lime to pH above 10; the lime dose is governed by the alkalinity, about 1.4 to 1.5 times it, not by the phosphorus (Metcalf and Eddy chapter 6)
    MgX2++NHX4X++POX4X3+6HX2OMgNHX4POX46HX2O(s)\ce{Mg^2+ + NH4^+ + PO4^3- + 6 H2O -> MgNH4PO4.6H2O (s)}
    struvite; theoretical Mg:N:P 1:1:1, optimum pH 8.5 to 9.0, inhibited below pH 7, above pH 11 other precipitates form and ammonia volatilises; raising Mg:P from 0.8 to 1.2 lifted phosphorus removal from 80.8 to 95.5 percent in one study
    HX3POX4HX2POX4X+HX+\ce{H3PO4 <=> H2PO4^- + H+}
    pKa1 about 2.1 at 25 C; phosphoric acid itself exists only in acid industrial liquor, which is why a fertiliser or metal finishing effluent needs neutralisation before any phosphate precipitation is attempted
    HPOX4X2POX4X3+HX+\ce{HPO4^2- <=> PO4^3- + H+}
    pKa3 about 12.3 at 25 C; the trivalent ion the precipitation equations are written with is a minority species even at lime softening pH, so the apparent stoichiometries are thermodynamic, not what the dosing pump sees
    PX3OX10X5+2HX2O3POX4X3+4HX+\ce{P3O10^5- + 2 H2O -> 3 PO4^3- + 4 H+}
    hydrolysis of tripolyphosphate from detergents and from sequestrant dosing; hours to days, faster warm and acid; until it happens the phosphorus is invisible to the orthophosphate test and is not precipitated by metal salts, which is why total phosphorus samples are digested first
    AlX2(SOX4)X314HX2O+2POX4X32AlPOX4(s)+3SOX4X2+14HX2O\ce{Al2(SO4)3.14H2O + 2 PO4^3- -> 2 AlPO4 (s) + 3 SO4^2- + 14 H2O}
    alum written as the commercial hydrate: 2 mol P per mol of alum in theory, 1.5 to 3 times the metal in practice because aluminium hydroxide forms in parallel; each mol of alum also delivers 3 mol of sulfate to the effluent
    3FeX2++2POX4X3FeX3(POX4)X2(s)\ce{3 Fe^2+ + 2 PO4^3- -> Fe3(PO4)2 (s)}
    vivianite in iron dosed anaerobic sludge and in digesters; the reason iron dosed upstream keeps phosphorus locked in the digested sludge instead of releasing it to the dewatering liquor, and the reason iron dosing and struvite recovery compete for the same phosphorus

    4 · Role in treatment

    as a problem
    eutrophication of receiving water
    phosphate as the limiting nutrient; algal blooms, oxygen depletion, loss of the lake
    the EU recast directive defines eutrophication as enrichment of water by nutrients, especially compounds of nitrogen or phosphorus; the element entry carries the same story
    struvite scaling in digesters and sludge lines
    digestion releases ammonium, magnesium and phosphate; carbon dioxide stripping at pumps and bends raises pH and struvite crystallises on pipe walls and centrifuges
    the mineral of the recovery reactor is the scale of the return line (Metcalf and Eddy chapter 15, from the chapter, not re-read)
    HCOX3XCOX2(g)+OHX\ce{HCO3^- -> CO2 (g) + OH-}
    carbon dioxide stripping wherever the digested sludge is agitated, pumped or dropped in pressure; the released hydroxide lifts pH into the struvite window at 8.5 to 9, which is why the scale grows at pump volutes, bends and centrifuges and not in the quiescent tank
    phosphorus return in sludge liquors
    EBPR sludge releases phosphorus again under anaerobic digestion; dewatering liquor recycles it to the head of the plant
    the reason struvite recovery is placed on the digester liquor
    phosphate interference on adsorbents
    competes with arsenate for iron hydroxide sites
    EPA arsenic manual figure quoted above
    phosphonate and phosphate residues in membrane concentrate
    antiscalant dosed to the feed leaves in the reject at the concentration factor; it counts toward total phosphorus in the discharge
    the CWW BAT-AEL lower end applies where phosphorus mainly comes from heating or cooling systems
    as a reagent
    phosphonate and polyphosphate antiscalants in reverse osmosis and cooling water
    sub stoichiometric threshold inhibition: a few mg/L adsorb on calcium carbonate and sulfate nuclei and block growth so that supersaturated concentrate does not scale
    a bisphosphonate (HEDP derivative) was dosed at 5 mg/L in the reverse osmosis case study read; the threshold mechanism is described in MWH chapter 17 (from the chapter, not re-read)
    orthophosphate and polyphosphate corrosion inhibitors and sequestrants in distribution
    orthophosphate forms protective films on lead and copper; polyphosphate sequesters iron and manganese so they do not stain before they reach the tap
    5PbX2++3POX4X3+OHXPbX5(POX4)X3OH(s)\ce{5 Pb^2+ + 3 PO4^3- + OH- -> Pb5(PO4)3OH (s)}
    WHO hardness document: soft or aggressive water is stabilised by adding corrosion inhibiting substances such as phosphates. The lead film is hydroxypyromorphite, written here from the lead chapter of this book, the lead analogue of hydroxyapatite; the same dose forms a copper phosphate film on copper pipe. The sequestrant use is the opposite chemistry: polyphosphate holds iron and manganese in solution until it hydrolyses
    phosphoric acid and phosphate salts as nutrient for industrial biological treatment
    phosphorus deficient industrial wastewater (pulp, petrochemical, food) needs added phosphate for biomass growth
    the CWW BAT-AEL footnote names phosphorus added for the proper operation of the biological plant as a reason for the lower end of the range
    trisodium phosphate for boiler water conditioning
    precipitates residual hardness as a non adherent sludge and buffers pH
    POX4X3+HX2OHPOX4X2+OHX\ce{PO4^3- + H2O <=> HPO4^2- + OH-}
    the element entry lists trisodium phosphate for boiler scale control; no dose read; the hydrolysis of the trivalent ion is what makes trisodium phosphate alkaline and is the buffering half of its job, the precipitation of residual hardness as calcium phosphate being the other

    5 · Removal and control

    chemical precipitation with aluminium or iron salts
    metal phosphate precipitation plus adsorption on the hydroxide floc; dosed to primary (pre-precipitation), to the aeration basin (simultaneous) or to the effluent before filters (post-precipitation)
    FeX3++HPOX4X2FePOX4(s)+HX+\ce{Fe^3+ + HPO4^2- -> FePO4 (s) + H+}
    pH 5.5 to 7; 1.5 to 3 mol metal per mol P in practice, more for the lowest effluent values; alkalinity consumed with the hydroxide
    Efficiency
    to 1 mg/L routinely; below 0.5 mg/L with tertiary filtration and higher metal ratios (Metcalf and Eddy chapter 6, from the chapter)
    Interferences
    organic and polyphosphate fractions are not precipitated until hydrolysed; sludge mass rises
    lime precipitation
    hydroxyapatite and calcium phosphate precipitation at high pH with CaCO₃ and Mg(OH)₂
    5CaX2++3POX4X3+OHXCaX5(POX4)X3OH(s)\ce{5 Ca^2+ + 3 PO4^3- + OH- -> Ca5(PO4)3OH (s)}
    pH above 10; lime dose set by alkalinity; recarbonation needed afterwards
    Efficiency
    not quoted
    Interferences
    large sludge volume
    enhanced biological phosphorus removal (EBPR)
    phosphorus accumulating organisms take up acetate and propionate anaerobically, storing them as PHB and releasing phosphate while consuming polyphosphate and glycogen; aerobically they grow, restore polyphosphate and replenish glycogen from the stored PHB; phosphorus leaves in the waste sludge
    an anaerobic zone ahead of the aerobic zone with enough volatile fatty acids; polyphosphate 4 to 15 percent of PAO dry biomass
    Efficiency
    not quoted as a general figure in the source read; the reactors studied gave 5.4 and 8.3 mg/L effluent phosphate from high influent phosphorus
    Interferences
    nitrate or oxygen in the anaerobic zone, low VFA, glycogen accumulating organisms, phosphorus release in digestion
    struvite crystallisation from digester liquor
    magnesium dosing and pH rise to 8.5 to 9 crystallise MgNH₄PO₄.6H₂O in a fluidised bed; the pellets are a slow release fertiliser
    MgX2++NHX4X++POX4X3+6HX2OMgNHX4POX46HX2O(s)\ce{Mg^2+ + NH4^+ + PO4^3- + 6 H2O -> MgNH4PO4.6H2O (s)}
    Mg:P above 1; pH 8.5 to 9.0 optimum
    Efficiency
    80.8 to 95.5 percent phosphorus removal as Mg:P rose from 0.8 to 1.2 in the study quoted
    Interferences
    calcium competes to form calcium phosphate; pH above 11 loses ammonia
    tertiary filtration and membrane polishing
    removes the particulate phosphorus that carries the residual after precipitation
    needed for the 0.5 mg/L class limits
    Efficiency
    not quoted
    Interferences
    soluble non reactive phosphorus passes

    6 · Analytics

    methodstandarddetection limitnote
    ascorbic acid molybdenum blue colorimetryStandard Methods 4500-P E (after 4500-P B digestion for total P); ISO 6878; EPA 365 seriesISO 6878: 0.005 to 0.8 mg/L P without dilutionorthophosphate directly (reactive P); persulfate or acid digestion converts poly and organic P for total P; ZDHC lists ISO 6878, EPA 365.4 and SM 4500-P J for total phosphorus
    ion chromatographyISO 10304-1lower limit of application 0.1 mg/L orthophosphateorthophosphate only
    ICP-OES (total phosphorus)EPA 200.7 (214.914 nm); ISO 11885EPA 200.7 instrument detection limit 76 µg/L, total recoverable method detection limit 0.06 mg/Lno speciation; phosphorus is not an analyte of EPA 200.8 (ICP-MS)
    Sampling pitfalls
    Filter 0.45 µm at once for dissolved reactive phosphorus; unfiltered samples convert particulate and polyphosphate to orthophosphate on standing. Acidify or freeze samples for total phosphorus. Phosphate contamination from detergent washed glassware is the classic blank problem; phosphate free detergents and acid rinsed glass are standard.

    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 chemical fact sheet for phosphate exists on the WHO fact sheet path
    EU DWD 2020/2184not set phosphorus is not in Annex I
    US EPAnot regulated absent from the primary and secondary standards
    discharge
    bodylimitnote
    EU UWWTD 91/271/EEC, Annex I Table 2 (sensitive areas)2 (10,000 to 100,000 p.e.); 1 (more than 100,000 p.e.) mg/L P
    superseded progressively by the 2024 recast
    annual mean total phosphorus, or a minimum reduction of 80 percent; molecular absorption spectrophotometry as reference method
    EU UWWTD 2024/3019 (recast), Annex I Table 2 (tertiary treatment)0.7 (10,000 to below 150,000 p.e.); 0.5 (150,000 p.e. and above) mg/L P
    time-sensitive: Article 7 plant level deadlines were not captured this session
    or minimum reduction 87.5 and 90 percent; national load reduction targets of at least 75 percent of total phosphorus from 1 January 2025, 82.5 percent by 31 December 2039 and 87.5 percent by 31 December 2045; tertiary treatment is imposed on all plants of 150,000 p.e. and above and on 10,000 p.e. and above in eutrophication sensitive areas
    EU CWW BREF BAT-AEL (Decision 2016/902), total phosphorus0.50 to 3.0 mg/Lapplies if the emission exceeds 300 kg/yr; the lower end is typically achieved when phosphorus is added for the biological plant or originates mainly from heating or cooling systems
    EU textiles BAT conclusions (Decision 2022/2508), total phosphorus, direct discharge0.4 to 2 mg/L
    footnotes on applicability not read
    BAT-AEL as daily average
    US EPA 40 CFR effluent guidelinesnot set other categories not readno phosphorus limit in the categories read this session (410, 423, 425, 433, 434); phosphorus limits in the US are set in NPDES permits against state nutrient criteria
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)2.0 mg/L as P
    region-dependent; marine discharge only
    Table 1 phosphate (as P) maximum allowable concentration
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewer50 mg/L
    region-dependent; sewer discharge
    Table A₂ total phosphorus maximum allowable concentration
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022), total phosphorus3 foundational; 0.5 textile and 1 leather progressive; 0.1 textile and 0.5 leather aspirational mg/Lmethods ISO 17294, ISO 11885, ISO 6878, EPA 365.4, SM 4500-P J, EPA 200.7 and 200.8

    8 · Health and environmental effects

    Toxicity
    Orthophosphate in water is not a health concern at any level found; a person eats about 1 g of phosphate a day. White phosphorus, 50 mg fatal, is the toxic form and does not occur in water (the element entry).
    Bioaccumulation
    Phosphorus is taken up by every organism as nutrient; there is no bioaccumulation hazard in the toxicological sense.
    Ecotoxicity
    Eutrophication is the effect: phosphate is the limiting nutrient of most lakes and rivers, so discharge limits are set on ecology, not toxicity. The US EPA aquatic life table carries only elemental phosphorus (1986) with no criterion values; nutrient criteria are ecoregional and were not read.

    Flags

    • The 4 to 12 mg/L municipal wastewater range is a Metcalf and Eddy typical composition table cited from memory of chapter 3.
    • The phosphate pKa values, the metal to phosphorus dosing ratios, the lime dose rule and the struvite scaling statement are textbook chapters not re-read this session.
    • The 2024 UWWTD Article 7 deadlines for tertiary treatment by plant size were not captured; the national load reduction dates are from Article 10 as read.
    • The textile BAT-AEL footnotes on when the phosphorus value applies were not read.
    • The antiscalant chemistry rests on one case study (a bisphosphonate at 5 mg/L) and a textbook chapter; typical HEDP and ATMP doses and the German drinking water limit seen in search summaries were not read and are not quoted.
    • The EBPR effluent figures quoted are from a laboratory study with high influent phosphorus, not a full scale plant.
    • Abu Dhabi values cover two media and two parameters (marine phosphate as P 2.0 mg/L, sewer total phosphorus 50 mg/L).

    Gaps

    • No source read gives phosphorus in groundwater, surface water or specific industrial effluents; the eutrophication threshold concentrations were not sourced.
    • EPA Nutrient Control Design Manual (2010) could not be opened (file too large for the fetch tool); Metcalf and Eddy chapters stand in.
    • Typical antiscalant doses and phosphonate limits for drinking water production were not read.
    • The US ecoregional nutrient criteria and the EPA 1986 Gold Book phosphorus recommendations were not read.
    • The Standard Methods 4500-P E detection limit was not read; the ISO 6878 range stands in.
    • Other GCC discharge standards (Saudi, Oman, Qatar) were not read.
    • No solubility products for AlPO₄, FePO₄, hydroxyapatite, vivianite or struvite were read. The phosphoric acid pKa ladder is from Stumm and Morgan chapter 3 and the alum, vivianite and polyphosphate stoichiometries from Metcalf and Eddy chapters 3 and 6, from the chapter, not re-read.
    • No balanced equation is written for enhanced biological phosphorus removal: the anaerobic release and aerobic uptake steps involve acetate, PHB, glycogen and intracellular polyphosphate of no fixed formula, and no source read prints a stoichiometry.

    Sources

    Council Directive 91/271/EEC concerning urban waste water treatment, Annex I Table 2
    Directive (EU) 2024/3019 concerning urban wastewater treatment (recast), Articles 7 and 10 and Annex I Table 2
    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
    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)
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), conventional parameters, anions and metals tables and sludge Table 4A
    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
    40 CFR 433.15, Pretreatment standards for existing sources (PSES), metal finishing point source category
    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, National Primary Drinking Water Regulations (table of MCLs and treatment techniques)
    WHO GDWQ 4th ed. with addenda (2022), chapter 12 chemical fact sheets on the WHO fact sheet path (no phosphate sheet exists at that path)
    WHO, Hardness in Drinking-water, background document, WHO/HSE/WSH/10.01/10/Rev/1 (2011), sections 1.1 to 1.3, 2.1, 4.2 and 4.3
    Wu S. et al., Effects of physicochemical parameters on struvite crystallization based on kinetics, International Journal of Environmental Research and Public Health 19(12), 7204 (2022), doi 10.3390/ijerph19127204
    Xing W. et al., Dynamics of intracellular polymers in enhanced biological phosphorus removal processes under different organic carbon concentrations, BioMed Research International 2013, 761082, doi 10.1155/2013/761082, introduction
    Popov K. et al., A case study of calcium carbonate crystallization during reverse osmosis water desalination in presence of novel fluorescent-tagged antiscalants, Membranes 12(2), 194 (2022), doi 10.3390/membranes12020194
    US EPA, National Recommended Water Quality Criteria, Aquatic Life Criteria Table (phosphorus elemental, 1986, no values)
    Standard Methods (online edition), 4500-P Phosphorus (B. digestion, E. ascorbic acid method)
    ISO 6878:2004, Water quality. Determination of phosphorus. Ammonium molybdate spectrometric 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
    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)
    ISO 11885:2007, Water quality. Determination of selected elements by inductively coupled plasma optical emission spectrometry (ICP-OES)
    PubChem element summary for phosphorus; estimated oceanic abundance 6 x 10^-2 mg/L (PUG View, reference 5, Jefferson Lab)
    The Element Book, layer 1 entry for phosphorus (data/elements/P.json and data/reference/text/P.json)
    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 3 (acids and bases: phosphoric acid dissociation)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 3 (wastewater composition), chapter 6 (chemical precipitation of phosphorus), chapter 8 (enhanced biological phosphorus removal) and chapter 15 (nutrient recovery, struvite)
    Crittenden, J. C. et al., MWH's Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 17 (reverse osmosis: scaling and antiscalants)

    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.