Hydrogen

    group 1 · period 1 · s-block · diatomic nonmetal

    fullHydrogen is the water in water treatment: the H+ activity that pH measures sets corrosion, scaling, coagulation, disinfection and every acid base equilibrium in the plant, pH is an indicator parameter in the EU, a secondary standard in the US and a permit condition on nearly every discharge, and dissolved hydrogen gas is the electron donor of anaerobic and reductive processes and a by-product of electrolysis and corrosion.

    Typical wastewaters

    • hydrofluoric acid, ammonia fertiliser, primary beryllium and semiconductor plant effluent free mineral acidity as H+ (or alkalinity as OH-) in process wastewater, neutralised to the 6.0 to 9.0 pH band that footnote 1 of each US effluent guideline table sets
    • acid mine drainage and metal pickling H+ as free acidity with sulfate or chloride, neutralised with lime, caustic soda or magnesium hydroxide to the permit band; metals precipitate as hydroxides in the same step and gypsum sludge forms with lime and sulfuric acid no acid effluent concentrations were read
    • alkaline discharges (lime, caustic soda, concrete washwater) OH- alkalinity at high pH, neutralised with sulfuric acid or carbon dioxide (CO₂ cannot overshoot below about pH 6 in buffered water)
    • municipal sewage (secondary treatment effluent) pH held in the 6.0 to 9.0 band by the biological process itself; the band US secondary treatment effluent must stay within
    • textile dyeing and finishing and leather tanning pH measured on site, 6 to 9 at every ZDHC level; the same band at Foundational, Progressive and Aspirational
    In the ledger's plant and process records, discharged by: Fruit and vegetables (Food and beverage) · Starch production (Food and beverage) · Brewing (Food and beverage) · Oilseed processing and vegetable oil refining (Food and beverage) · Sugar manufacturing (Food and beverage) · Wine production (Food and beverage) · Grain milling (Food and beverage) · Olive oil processing and refining (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) · Dairies (Food and beverage) · Ethanol production (Food and beverage) · Meat processing (Food and beverage) · Cyanides (sodium and potassium cyanide) (Chemicals) · Ethanolamines (Chemicals) · NPK and CN fertilisers (Chemicals) · Nitric acid (Chemicals) · Polyamides (PA 6, PA 66) and their spinning (Chemicals) · Speciality inorganic pigments (iron oxide, chromium oxide, CIC, zinc sulphide, lithopone) (Chemicals) · Sulphuric acid (Chemicals) · Superphosphates (Chemicals) · Abrasion peeling (Food and beverage) · Animal feed (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) · 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) · 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) · 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) · Soft drinks and nectar/juice (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) · Halogenation (Pharmaceuticals) · N-acylation (Pharmaceuticals) · Phosgenation (Pharmaceuticals) · Sulphochlorination with chlorosulphonic acid (Pharmaceuticals) · Sulphonation (Pharmaceuticals) · Sulphonation with SO3 (Pharmaceuticals) · Desizing (Textile) · Easy-care finishing (Textile) · Mothproofing and antimicrobial finishing (Textile)

    1 · Identity

    Symbol, number
    H, 1
    Oxidation states in water
    +1 in water itself, in the hydrated proton (written H+ here, H₃O⁺ in reality) whose activity pH measures, in every acid, and bonded to carbon, nitrogen and oxygen in dissolved organic matter and ammonia; 0 as dissolved hydrogen gas H₂, released by electrolysis, by the cathodic reaction of corrosion in acid or anoxic water and by fermentation, and consumed by hydrogenotrophic bacteria; -1 (hydride) does not exist in water, hydrides react with it to give H₂ (book entry).
    Note
    The element entry already carries combustion, the H₂ and Cl₂ chain reaction and the hydride chemistry. This chapter is about pH and about H₂ as a reagent and by-product. Hydrogen sulfide belongs to the sulfur chapter and hydrogen peroxide to the oxygen chapter; the carbonate buffer that fixes the pH of most natural water is written out in the carbon chapter and only referenced here.

    2 · Occurrence in water

    Natural sources
    The pH of most natural and drinking water is controlled by the carbon dioxide, bicarbonate and carbonate equilibrium: more dissolved CO₂ lowers pH, less raises it, and temperature shifts the equilibria (pure water falls about 0.45 pH unit for a 25 C rise). Acid rain gives lower pH, limestone catchments higher (WHO background document). Dissolved H₂ is produced by fermentation in anoxic sediments and anaerobic digesters, where it is an intermediate consumed by hydrogenotrophic methanogens (Metcalf and Eddy chapter 10).
    Anthropogenic sources
    Acid discharges (mine drainage, metal pickling, acid plants) and alkaline discharges (lime, caustic soda, concrete washwater, insufficiently cured cement mortar pipe linings, which WHO names as a cause of extreme pH); treatment chemicals that consume or release protons, the acid coagulants and chlorine gas among them; H₂ from water electrolysers and from on-site electrolytic hypochlorite generation; H₂ evolved on steel in anoxic water and on cathodically protected structures.
    matrixtypical rangenote
    drinking water, pH6.5 to 8.5 pH unitsthe range within which the pH of most drinking water lies; natural waters are lower with acid rain and higher in limestone areas
    drinking water, operational optimum pH6.5 to 9.5 pH unitsthe optimum varies with the water and the pipe materials but is often in this range; chlorine disinfection prefers below 8.0
    treated municipal wastewater, pH6.0 to 9.0 pH unitsa permit band, not a surveythe band that US secondary treatment effluent must stay within, so also the band in which biological plants are run
    textile and leather effluent, pH6 to 9 pH unitsa limit, not a surveythe ZDHC band for all three levels; measured on site
    dissolved H₂, any waternot quantified no source read gives dissolved hydrogen concentrations; it is a trace gas in oxic water and transient in anoxic water

    3 · Speciation

    pH is the negative common logarithm of the hydrogen ion activity, which equals the concentration in dilute solution (WHO background document). Water dissociates to H+ and OH- with an ion product of 10⁻14 at 25 C, so pH 7 is neutral only at that temperature; the ion product rises with temperature and neutral pH falls (Stumm and Morgan chapter 3). In almost every natural water the free proton is a minor species and pH is set by the weak acid systems that buffer it: carbonic acid and bicarbonate between pH 6 and 9, ammonia above 9, hydroxide above 10 (carbon and nitrogen chapters). Dissolved H₂ is a sparingly soluble, unreactive gas at room temperature that only bacteria and electrodes use.

    conditiondominant speciesnote
    pH below 4.5free H+ with mineral acid anions; no bicarbonate alkalinitythe endpoint of the total alkalinity titration; acid mine drainage and pickling rinses sit here
    pH 6 to 9, the range of nearly all natural and treated waterH+ at 10⁻6 to 10⁻9 mol/L, buffered by H₂CO₃, HCO₃⁻ and CO₃²⁻the carbonate system is written out in the carbon chapter
    pH above 10OH- and CO₃²⁻ dominate; NH₃ rather than NH₄⁺lime softening, lime stabilised sludge, ammonia stripping
    anoxic water with fermentation or corroding steeldissolved H₂consumed within hours to days by methanogens, sulfate reducers or denitrifiers; escapes as gas from digesters
    Solubility
    Not applicable to H+; the solubility of H₂ in water is not quoted because no source read prints it (it is a sparingly soluble gas).
    Hydrolysis
    Water is the hydrolysis: H₂O splits to H+ and OH- and every other hydrolysis in the book (Fe³⁺, Al³⁺, chlorine, coagulants) is the transfer of one of those ions.
    Complexation
    H+ competes with every metal for ligands, so lowering pH frees metals from hydroxide, carbonate and organic complexes; that is why acidification preserves metal samples and why acid water carries metals (WHO pH document: the lower the pH, the higher the potential corrosion).
    Precipitates
    None of hydrogen itself. pH decides which hydroxides and carbonates precipitate and at what pH, treated under each metal.
    HX2OHX++OHX\ce{H2O <=> H+ + OH-}
    ion product Kw 10^-14 at 25 C; pH plus pOH equals 14 at that temperature; Kw rises with temperature so the neutral point moves below 7 in warm water
    COX2+HX2OHX++HCOX3X\ce{CO2 + H2O <=> H+ + HCO3^-}
    the reaction that sets the pH of most natural water; more CO2 lowers pH (WHO background document); constants in the carbon chapter
    2HX2O2HX2+OX2\ce{2 H2O -> 2 H2 + O2}
    electrolysis; the hydrogen and oxygen of water electrolysers and the cathode side of every electrochemical treatment cell
    NaCl+HX2ONaOCl+HX2\ce{NaCl + H2O -> NaOCl + H2}
    on-site electrochemical generation of dilute (below 1 percent) sodium hypochlorite from brine, as the EPA manual describes; the overall stoichiometry is written here from the electrochemistry, the manual names the process without printing it; the hydrogen must be vented
    Fe+2HX+FeX2++HX2\ce{Fe + 2 H+ -> Fe^2+ + H2}
    corrosion of steel in acid or anoxic water, written as the full reaction; the cathodic half reaction is the reduction of two protons to H2, and in oxic water the cathode reduces oxygen instead (oxygen chapter)
    HX2SOX4+2HCOX3XSOX4X2+2COX2+2HX2O\ce{H2SO4 + 2 HCO3^- -> SO4^2- + 2 CO2 + 2 H2O}
    acid dosing for pH control consumes bicarbonate alkalinity and releases CO2; one mol of strong acid destroys one equivalent of alkalinity
    4HX2+COX2CHX4+2HX2O\ce{4 H2 + CO2 -> CH4 + 2 H2O}
    hydrogenotrophic methanogenesis in anaerobic digestion; hydrogen partial pressure must stay low for the fermentation steps before it to proceed (Metcalf and Eddy chapter 10)

    4 · Role in treatment

    as a problem
    corrosion of mains and plumbing at low pH
    the lower the pH the higher the potential corrosion; metals from pipes and solder enter the water
    WHO background document; the health effect of pH is indirect, through metals and failed disinfection; US secondary standard lists corrosion and bitter metallic taste at low pH
    scale, deposits and slippery feel at high pH
    calcium carbonate and magnesium hydroxide precipitate as pH rises
    US secondary standard: slippery feel, soda taste, deposits
    disinfection efficiency
    hypochlorous acid, the germicide, dissociates to hypochlorite above pH 7.5
    WHO: for effective disinfection with chlorine the pH should preferably be below 8.0; the HOCl equilibrium is in the chlorine chapter
    coagulation and precipitation windows
    every coagulant and every hydroxide precipitate has a pH window; ferric salts 5 to 8, alum 5 to 7, enhanced coagulation target pH 5.5 to 7.5 by alkalinity
    the enhanced coagulation Step 2 target pH table of 40 CFR 141.135 runs from 5.5 (alkalinity 0 to 60) to 7.5 (above 240 mg/L as CaCO₃)
    un-ionised ammonia toxicity and stripping
    NH₃ rather than NH₄⁺ above pH 9.25
    nitrogen chapter
    membrane rejection of weak acids
    boric acid and other uncharged weak acids pass reverse osmosis unless pH is raised above their pKa
    boron chapter
    hydrogen gas from electrolytic cells
    on-site hypochlorite generators and electrolysers release H₂, which forms explosive mixtures with air
    the 4 to 74 percent explosive range in air is in the element entry; ventilation of cell rooms is the control (general practice, the EPA manual names the process only)
    as a reagent
    pH depression with sulfuric or hydrochloric acid
    strong acid converts bicarbonate to carbon dioxide; used before coagulation, ahead of reverse osmosis to hold calcium carbonate below saturation, and to neutralise alkaline effluent
    HX2SOX4+2HCOX3XSOX4X2+2COX2+2HX2O\ce{H2SO4 + 2 HCO3^- -> SO4^2- + 2 CO2 + 2 H2O}
    dose from the alkalinity titration; sulfuric acid adds sulfate, hydrochloric adds chloride
    pH elevation with lime, caustic soda or soda ash
    hydroxide neutralises acid and precipitates metals; the reagents are treated in the calcium and sodium chapters
    neutralisation of acid effluent to the 6 to 9 permit band; corrosion control of finished water
    carbon dioxide for recarbonation
    CO₂ lowers pH after lime softening without adding mineral acidity
    COX2+OHXHCOX3X\ce{CO2 + OH- -> HCO3^-}
    after lime softening at pH above 10; the carbonate system is in the carbon chapter
    hydrogen gas as electron donor
    hydrogenotrophic bacteria reduce nitrate to nitrogen gas with H₂ supplied through membranes, leaving no organic residual
    2NOX3X+5HX2+2HX+NX2+6HX2O\ce{2 NO3^- + 5 H2 + 2 H+ -> N2 + 6 H2O}
    Metcalf and Eddy chapter 7 lists hydrogen among the electron donors for denitrification; the stoichiometry is the electron balance
    limestone contactors for aggressive water
    soft acidic water dissolves calcium carbonate, gaining alkalinity, calcium and pH
    CaCOX3(s)+HX+CaX2++HCOX3X\ce{CaCO3 (s) + H+ -> Ca^2+ + HCO3^-}
    corrosion control of low alkalinity supplies (MWH chapter 22)

    5 · Removal and control

    neutralisation of acid effluent
    lime, caustic soda or magnesium hydroxide slurry dosed under pH control; metals precipitate as hydroxides at the same time
    HX2SOX4+Ca(OH)X2CaSOX4+2HX2O\ce{H2SO4 + Ca(OH)2 -> CaSO4 + 2 H2O}
    to the 6.0 to 9.0 band of the discharge permit; gypsum sludge with lime and sulfuric acid
    Efficiency
    to the permit band
    Interferences
    poor mixing and slow lime dissolution give pH swings; equalisation first
    neutralisation of alkaline effluent
    sulfuric acid or carbon dioxide
    COX2+OHXHCOX3X\ce{CO2 + OH- -> HCO3^-}
    CO2 cannot overshoot below about pH 6 in buffered water and adds no salt; acid is faster and cheaper
    Efficiency
    to the permit band
    pH adjustment as a treatment step
    pH is not removed but set: before coagulation, before precipitation, before disinfection and before distribution
    WHO: careful attention to pH control is necessary at all stages of treatment to ensure clarification and disinfection, and the pH entering distribution must be controlled to minimise corrosion
    Efficiency
    not applicable
    hydrogen gas
    vented or diluted below the explosive range; not a water contaminant
    electrolytic cells and digester gas
    Efficiency
    not applicable

    6 · Analytics

    methodstandarddetection limitnote
    pH by glass electrodeStandard Methods 4500-H+ B; ISO 10523; EPA 150.1not applicable; resolution 0.01 pH unit with temperature compensationthe electrometric method is the only one ZDHC accepts; WHO: temperature has a significant effect on the measurement
    dissolved hydrogenno standard method readnot readgas chromatography of headspace in research on anaerobic reactors; not a routine parameter
    Sampling pitfalls
    Measure pH on site: loss or gain of carbon dioxide in the bottle shifts it, and temperature changes both the equilibrium and the electrode response (WHO background document, APHA). Calibrate with two buffers bracketing the sample. In low ionic strength water the glass electrode drifts; use a low ionic strength electrode or add a neutral salt. Report the temperature with every pH.

    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 health based guideline value; one of the most important operational water quality parameters; the background document puts the optimum often at 6.5 to 9.5 and chlorination preferably below 8.0
    EU DWD 2020/21846.5 to 9.5 pH unitsAnnex I Part C indicator parameter; the water should not be aggressive; still bottled water may go down to 4.5 and carbonated bottled water lower
    US EPA6.5 to 8.5 pH unitsNational Secondary Drinking Water Regulation, non enforceable; low pH bitter metallic taste and corrosion, high pH slippery feel, soda taste, deposits
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set pH is not among the BAT 12 parameters; it is a permit condition in every Member State
    EU UWWTD 2024/3019not set Annex I Table 1 covers BOD₅, COD, TOC and TSS, Table 2 nitrogen and phosphorus; no pH value
    US EPA 40 CFR 133.102(c), secondary treatment6.0 to 9.0 pH unitsunless the works adds no inorganic chemicals and industrial contributions do not cause the excursion
    US EPA effluent guidelines, industrial categories (40 CFR 415.82 hydrofluoric acid, 418.22 ammonia, 421.152 primary beryllium, 469.14 semiconductors)6.0 to 9.0 pH unitsthe same band appears as footnote 1 in each table read
    Abu Dhabi ADS 23/2017, discharge to the marine environment (EAD)6.0 to 9.0 pH units
    region-dependent; marine discharge only
    Table 1
    Abu Dhabi DoE Trade Effluent Control Regulations 2022, discharge to sewerabove 6 and below 9 pH units
    region-dependent; sewer discharge
    Table A₁
    industry thresholds
    sectorbodylimitnote
    textile and leatherZDHC Wastewater Guidelines v₂.1 (2022)6 to 9 pH unitsTable 3, same at Foundational, Progressive and Aspirational; electrometric method on site

    8 · Health and environmental effects

    Toxicity
    pH alone is not the primary determinant of adverse effects; acids and alkalis in water are extremely dilute and stomach fluid is pH 1 to 3.5; any health effect is indirect, through metals leached from plumbing and inadequate disinfection (WHO background document). Hydrogen gas is not toxic and acts only as an asphyxiant and an explosion hazard (element entry).
    Bioaccumulation
    Not applicable.
    Ecotoxicity
    US EPA national recommended criteria: freshwater pH 6.5 to 9, saltwater 6.5 to 8.5, and open ocean pH not changed more than 0.2 unit from natural variation (1986 Gold Book, cited in the criteria table). pH also governs the toxicity of ammonia, aluminium and metals, which is why their criteria are pH dependent.

    Flags

    • The pH ranges given as concentrations are regulatory bands and a WHO generalisation, not surveys.
    • The on-site hypochlorite and hydrogenotrophic denitrification equations are written from the electrochemistry and electron balance; the EPA manual and Metcalf and Eddy name the processes without printing them.
    • Kw and the temperature dependence are cited to Stumm and Morgan chapter 3 from memory of the text, not re-read this session.
    • The 40 CFR industrial pH band is cited to the four sections read; other categories were not checked.
    • Abu Dhabi values cover two media (marine outfall 6.0 to 9.0, sewer above 6 and below 9); other GCC states were not read.

    Gaps

    • No source read gives dissolved hydrogen concentrations in any water matrix.
    • The solubility of H₂ and the temperature dependence of Kw are not quoted as numbers; Stumm and Morgan has them but was not re-read.
    • No survey of pH in municipal or industrial wastewater was read; permit bands stand in for it.
    • The 2016 CWW BREF text on pH neutralisation techniques was not re-read.
    • Other GCC discharge standards (Saudi, Oman, Qatar) were not read.

    Sources

    WHO Guidelines for Drinking-water Quality, 4th ed. incorporating the first and second addenda (2022), chapter 12 chemical fact sheet, pH (p. 452)
    WHO, pH in Drinking-water, revised background document for development of WHO Guidelines for Drinking-water Quality, WHO/SDE/WSH/07.01/1 (2007)
    Directive (EU) 2020/2184 on the quality of water intended for human consumption (recast), Annex I Parts B and C
    US EPA, Secondary Drinking Water Standards: Guidance for Nuisance Chemicals
    40 CFR 133.102, Secondary treatment (BOD5, suspended solids, pH)
    40 CFR 415.82, Hydrofluoric acid production subcategory BPT (pH footnote), with the same footnote read at 418.22, 421.152 and 469.14
    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
    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, National Recommended Water Quality Criteria, Aquatic Life Criteria Table
    US EPA, Alternative Disinfectants and Oxidants Guidance Manual, EPA 815-R-99-014 (April 1999), section 2.7.2.2 (on-site generation of sodium hypochlorite)
    Stumm, W. and Morgan, J. J., Aquatic Chemistry, 3rd ed. (Wiley, 1996), chapter 3 (acids and bases, ion product of water) and chapter 8 (redox, hydrogen half reaction)
    Snoeyink, V. L. and Jenkins, D., Water Chemistry (Wiley, 1980), chapter 4 (acid base chemistry, alkalinity and acid dosing)
    Metcalf and Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed. (McGraw-Hill, 2014), chapter 7 (biological denitrification electron donors) and chapter 10 (anaerobic digestion, hydrogen intermediate)
    MWH, Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 22 (internal corrosion, recarbonation and limestone contactors)
    The Element Book, entries for hydrogen (electrolysis of water, explosive range, hydrides) (data/elements/H.json, data/reference/text/H.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.