Silicon

    group 14 · period 3 · p-block · metalloid

    fullSilicon is not regulated in drinking water anywhere in the EU, US or WHO framework, but dissolved silica is the scaling constituent that caps reverse osmosis recovery, fouls boilers and cooling systems and resists every cheap removal process; silica sand is also the filter medium of the trade.

    Typical wastewaters

    • reverse osmosis concentrate monosilicic acid H₄SiO₄ concentrated past the 120 to 150 mg/L as SiO₂ solubility ceiling, polymerising to colloidal silica and metal silicates; up to 340 mg/L reported with inhibition and dispersion
    • demineraliser anion resin regenerant silicate in warm spent caustic; silica is the last anion loaded and the first to leak from strong base resin
    • semiconductor oxide chemical mechanical polishing (CMP) wastewater colloidal silica abrasive particles, destabilised and settled above 520 nm mean size by electrocoagulation
    • geothermal brine (separated water for reinjection) monomeric silicic acid about 420 ppm SiO₂ at Dieng, polymerising to scale; seeded precipitation at pH 7 and 40 C
    • cooling tower blowdown dissolved silica Si(OH)₄ with calcium and magnesium; 0.4 to 0.5 mol silica removed per mol iron or aluminium in electrocoagulation
    • solar panel manufacturing wastewater silicate ion together with germanium ion in actual solar panel wastewater
    In the ledger's plant and process records, discharged by: Phosphoric acid (wet process) (Chemicals)

    1 · Identity

    Symbol, number
    Si, 14
    Oxidation states in water
    +4 only, as monosilicic acid Si(OH)₄ (written H₄SiO₄), its anion H₃SiO₄⁻ above pH 9.9, polysilicic acids, colloidal and particulate silica, and metal silicates; analysts report all of it as SiO₂.
    Note
    The element entry gives the crust, the furnace and the properties narrative already says silica travels as dissolved silica and silicate and that sand is the filtration medium. This chapter is the scaling story: the 120 to 150 mg/L solubility ceiling and what it does to membranes.

    2 · Occurrence in water

    Natural sources
    Weathering of silicate minerals releases monosilicic acid to every natural water; groundwater in volcanic and geothermal terrain carries the most. Diatoms strip it from surface water in spring (the element entry).
    Anthropogenic sources
    Semiconductor chemical mechanical polishing wastewater and glass making carry colloidal silica; reverse osmosis concentrate and cooling tower blowdown concentrate natural silica several fold; silicate corrosion inhibitors and detergents (water glass) add silicate to sewage. No concentrations were read for these streams.
    matrixtypical rangenote
    natural water, general1 to 40 mg/L as SiO2up to nearly 100 mg/L in some geographic areas
    drinking water supplies, Western Australia (2019 to 2020)0.6 to 90 mg/L as SiO2
    region-dependent; Australian supplies
    means of various supply systems; Northern Territory systems averaged 11 to 104 mg/L
    seawater2.2 mg/L as Si
    single figure; surface ocean is depleted by diatoms
    estimated oceanic abundance, Jefferson Lab figure via PubChem, as in the element entry (about 4.7 mg/L as SiO₂)
    reverse osmosis concentrateup to 340 mg/L as SiO2single plant figurereject stream of a high recovery industrial plant run with scale inhibition and dispersion; the usual design ceiling is 120 to 150 mg/L

    3 · Speciation

    Below pH 9 dissolved silica is the uncharged monomer H₄SiO₄, which is why it passes anion exchangers weakly, is barely rejected by charge and cannot be precipitated as a simple salt. Its first pKa is 9.9, so only above pH 10 does the silicate anion dominate and solubility climb steeply. When the monomer exceeds about 2 mmol/L (120 to 150 mg/L as SiO₂ at 25 C) it polymerises to polysilicic acid and colloidal silica, fastest at neutral to slightly alkaline pH and slowest above 9.5 or below 6.5; calcium and above all magnesium accelerate polymerisation and precipitate metal silicates. Analysts distinguish reactive (molybdate) silica from total silica, the difference being the colloidal fraction.

    conditiondominant speciesnote
    natural water, pH 6 to 9, below saturationH₄SiO₄ monomer (reactive silica)uncharged; the form measured by the molybdate colour
    pH above 10H₃SiO₄⁻ and, near pH 12, H₂SiO₄²⁻solubility rises sharply; the basis of high pH reverse osmosis operation and of caustic membrane cleaning
    supersaturated concentrate, neutral pHpolysilicic acid, colloidal silica, amorphous silica scale on the membranepolymerisation is fastest here
    hard water at high pHmagnesium and calcium silicates, hydroxyaluminosilicates, iron silicatesthe reason softening removes silica and the reason RO scale is often a mixed metal silicate
    Solubility
    Crystalline silica (quartz) about 5 to 6 mg/L; amorphous silica 120 to 150 mg/L at 25 C, roughly constant up to pH 9 and rising dramatically above pH 10; solubility rises with temperature and falls with the presence of calcium, magnesium and some salts. Australian guidance quotes 100 to 140 mg/L for amorphous silica and about 6 mg/L for crystalline.
    Hydrolysis
    Monosilicic acid is a very weak acid, pKa 9.9 for the first dissociation; local pH rise inside a strong base anion resin is what lets it exchange at all.
    Complexation
    Silicate binds aluminium and iron hydroxide surfaces and competes with arsenate and fluoride on activated alumina and iron media (EPA arsenic manual, via the arsenic chapter); it forms hydroxyaluminosilicates in alum treated water.
    Precipitates
    Amorphous silica, magnesium silicate, calcium silicate, iron and aluminium silicates; silica coprecipitates on Mg(OH)₂ in lime softening.
    SiOX2(s)+2HX2OHX4SiOX4\ce{SiO2 (s) + 2 H2O <=> H4SiO4}
    dissolution and precipitation of amorphous silica, the ceiling that governs scaling: 120 to 150 mg/L as SiO2 at 25 C, roughly constant to pH 9 and rising steeply above pH 10; quartz sits far lower at 5 to 6 mg/L, so a sand bed does not feed the water
    HX4SiOX4HX3SiOX4X+HX+\ce{H4SiO4 <=> H3SiO4^- + H+}
    pKa 9.9 at 25 C; below pH 9 the monomer is essentially uncharged
    HX3SiOX4XHX2SiOX4X2+HX+\ce{H3SiO4^- <=> H2SiO4^2- + H+}
    the second dissociation, reached only near pH 12; the constant was not read, and below pH 10 both anions are negligible against the H4SiO4 monomer
    2HX4SiOX4HX6SiX2OX7+HX2O\ce{2 H4SiO4 -> H6Si2O7 + H2O}
    first step of polymerisation above about 2 mmol/L monomer; fast at neutral to slightly alkaline pH, minimum rate above pH 9.5 and below 6.5; catalysed by Mg^2+ and Ca^2+
    Mg(OH)X2(s)+HX4SiOX4MgSiOX3(s)+3HX2O\ce{Mg(OH)2 (s) + H4SiO4 -> MgSiO3 (s) + 3 H2O}
    lime or magnesium softening at pH 10 to 11; silica adsorbs on and reacts with freshly precipitated magnesium hydroxide (the review describes the mechanism; the equation is the simplest stoichiometry)
    MgX2++HX4SiOX4MgSiOX3(s)+2HX++HX2O\ce{Mg^2+ + H4SiO4 -> MgSiO3 (s) + 2 H+ + H2O}
    magnesium silicate scale in a membrane concentrate and in hot systems; the reaction releases acid, so it runs harder as pH rises and as magnesium concentrates; the review describes mixed metal silicate scale, the stoichiometry is written here
    SiOX2(s)+2OHXSiOX3X2+HX2O\ce{SiO2 (s) + 2 OH- -> SiO3^2- + H2O}
    caustic cleaning of a silica fouled membrane or resin, and the reason amorphous silica solubility climbs above pH 10; high pH converts the deposit to soluble silicate
    ROH+HX4SiOX4RHX3SiOX4+HX2O\ce{ROH + H4SiO4 -> RH3SiO4 + H2O}
    strong base anion resin in the hydroxide form, R the resin; the alkalinity inside the bead ionises the weak acid, which is the only reason an uncharged monomer exchanges at all; warm caustic is needed to drive it back off

    4 · Role in treatment

    as a problem
    silica scaling of reverse osmosis membranes
    concentration in the reject stream past the solubility ceiling, then monomer deposition, polymerisation on the membrane and precipitation of metal silicates; the glass like film is hard to clean and forces lower recovery
    industry practice limits concentrate silica to about 120 mg/L at 25 C (Australian guidelines quote the same figure); the review gives 120 to 150 mg/L; a feed of 40 mg/L therefore caps recovery near 65 to 70 percent without antiscalant, pH shift or pretreatment
    HX4SiOX4SiOX2(s)+2HX2O\ce{H4SiO4 -> SiO2 (s) + 2 H2O}
    deposition once the concentrate passes the amorphous silica ceiling of about 120 mg/L as SiO2 at 25 C; the monomer deposits, then polymerises on the membrane and takes metal silicates down with it
    boiler and turbine deposits
    silica concentrates in boiler water and volatilises with high pressure steam to deposit on turbine blades
    boiler water silica limits were not read this session; the statement is qualitative
    silica in demineralisers
    weakly ionised silica is the last anion taken and the first to leak from strong base anion resin as the bed exhausts
    the review describes exchange as dependent on the local pH rise inside the resin
    colloidal silica fouling
    polymeric and colloidal silica are not measured by the molybdate test and foul membranes and ion exchange beds as particles
    total minus reactive silica is the operative measurement
    competition on adsorbents
    silicate competes with arsenate and fluoride on activated alumina and iron media at pH 7 to 9
    problem level 50 mg/L silica for activated alumina in the EPA arsenic manual (via the arsenic chapter)
    as a reagent
    silica sand and gravel as filter media
    granular quartz bed retains floc and particles by straining and attachment; anthracite and sand in dual media beds
    the element entry notes sand and gravel as the standard filtration media; 440 million tonnes of industrial silica sand a year
    activated silica as coagulant aid
    partly neutralised sodium silicate forms polysilicate anions that strengthen and weight alum floc
    MWH chapter 9 lists it among coagulant aids (from the chapter, not re-read)

    5 · Removal and control

    lime or lime-magnesium softening at high pH
    silica adsorbs on and reacts with freshly precipitated Mg(OH)₂; magnesium oxide or sodium aluminate is added when the raw water lacks magnesium
    Mg(OH)X2(s)+HX4SiOX4MgSiOX3(s)+3HX2O\ce{Mg(OH)2 (s) + H4SiO4 -> MgSiO3 (s) + 3 H2O}
    optimum pH 10 to 11 for adsorption on Mg(OH)2; feasible when the water has enough hardness to make the magnesium hydroxide; sludge and added salinity are the operating costs
    Efficiency
    more than 95 percent under adequate pH adjustment
    Interferences
    low magnesium water; calcium alone is much less effective
    coagulation with iron, aluminium or zinc salts
    adsorption on the metal hydroxide, charge neutralisation, enmeshment and bridging
    removal rises with pH from 5.5 to 10.5 at optimised dose
    Efficiency
    not quoted as a single figure
    Interferences
    sludge and conductivity increase
    electrocoagulation
    sacrificial aluminium or iron anodes generate the hydroxide in situ
    reverse osmosis pretreatment
    Efficiency
    up to 80 percent at 80 to 120 mg/L total silica in the case reported
    Interferences
    electrode passivation, energy
    seed precipitation
    supersaturated silica polymerises onto silica seed particles instead of the membrane
    ambient temperature, neutral pH; iron at 100 mg/L helped in the study quoted
    Efficiency
    700 mg/L silicic acid reduced to 100 to 150 mg/L
    Interferences
    slow kinetics
    strong base anion exchange (demineralisation)
    the weak acid ionises in the alkaline resin and exchanges; regenerated with caustic
    ROH+HX4SiOX4RHX3SiOX4+HX2O\ce{ROH + H4SiO4 -> RH3SiO4 + H2O}
    last anion loaded, first to leak; warm caustic regeneration
    Efficiency
    not quoted
    Interferences
    polymerised silica stays on the resin
    adsorption on activated alumina
    silicate exchanges on the alumina surface
    strongly pH dependent
    Efficiency
    about 90 percent at the optimum pH range in the study quoted
    Interferences
    calcium and magnesium also adsorb
    reverse osmosis with antiscalant, pH shift or intermediate softening
    the membrane rejects silica; recovery is limited by concentrate solubility, which antiscalants and dispersants, high or low pH operation and softening of the concentrate between stages extend
    high pH raises solubility and rejection (Australian guidelines); the review reports reject streams to 340 mg/L with inhibition and dispersion
    Efficiency
    silica rejection itself is high; the limit is recovery, not rejection
    Interferences
    hardness and iron precipitate silicates; colloidal silica fouls regardless of solubility

    6 · Analytics

    methodstandarddetection limitnote
    molybdosilicate colorimetry (reactive silica)Standard Methods 4500-SiO₂ C; ISO 16264 (flow analysis)ISO 16264 range 0.2 to 20 mg/L as SiO₂; Australian limits of reporting 0.05 to 0.5 mg/L depending on methodmeasures monomeric and small oligomeric silica; polymeric and colloidal silica are missed unless digested
    ICP-OES (total silica)EPA 200.7 (251.611 nm); ISO 11885EPA 200.7 instrument detection limit 26 µg/L as SiO₂, total recoverable method detection limit 0.02 mg/Lsilica is a listed analyte of EPA 200.7 but not of EPA 200.8 (ICP-MS), whose Table 1 lists 21 elements without silicon; glassware contaminates low level silica samples
    total minus reactive silicadifference methodnot applicablethe colloidal fraction that matters for membranes
    Sampling pitfalls
    Use plastic bottles, never glass, for silica; do not acidify below pH 2 for reactive silica or polymerised silica will not depolymerise in time; analyse promptly because supersaturated samples polymerise in the bottle and reactive silica falls. Report as SiO₂ or as Si and say which (SiO₂ is 2.14 times Si).

    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 silica or silicon was found on the WHO fact sheet path
    EU DWD 2020/2184not set silicon and silica are not in Annex I
    US EPAnot regulated absent from the primary and secondary drinking water standards
    Australian Drinking Water Guidelines (NHMRC)100 mg Si/L health (210 mg/L as SiO₂); 80 aesthetic mg/L as SiO2aesthetic value 80 mg/L as SiO₂ (37 mg Si/L) for scaling; health value from a rat NOAEL of 2,500 mg SiO₂/kg/day
    discharge
    bodylimitnote
    EU CWW BREF BAT-AEL (Decision 2016/902)not set silica is not a BAT 12 parameter
    Abu Dhabi ADS 23/2017 (marine) and DoE Trade Effluent Control Regulations 2022 (sewer)not set region-dependentsilica is not listed in either table
    industry thresholds
    sectorbodylimitnote
    textileZDHC Wastewater Guidelines v₂.1 (2022)not set silica is not a ZDHC parameter

    8 · Health and environmental effects

    Toxicity
    Ingested silica is essentially non toxic; the Australian health value rests on a rat NOAEL of 2,500 mg SiO₂/kg/day. The hazard of silicon is inhaled crystalline dust (silicosis), not water (the element entry).
    Bioaccumulation
    Diatoms and plants take up silicic acid to build silica frustules and phytoliths; no accumulation concern in animals is reported in the sources read.
    Ecotoxicity
    No US EPA aquatic life criterion; dissolved silica is a nutrient that limits diatom growth in lakes and coastal water rather than a toxicant.

    Flags

    • The 1 to 40 mg/L natural water range and the solubility figures are from a 2020 review; the Australian guideline gives 100 to 140 mg/L for amorphous silica solubility, the review 120 to 150 mg/L.
    • The seawater figure is a single PubChem abundance figure expressed as Si.
    • The boiler and turbine deposit statement is qualitative and unsourced this session.
    • The magnesium silicate equation is the simplest stoichiometry for the softening mechanism the review describes; the review prints no equation.
    • The activated silica coagulant aid is cited to MWH chapter 9 from memory.
    • The 65 to 70 percent recovery cap for a 40 mg/L feed is arithmetic on the 120 to 150 mg/L ceiling, not a source figure.
    • Australian guideline values are quoted because no WHO, EU or US value exists; they are national.

    Gaps

    • No source read gives silica in municipal wastewater, cooling tower blowdown or semiconductor wastewater as numbers.
    • Boiler water silica limits and steam carryover figures were not read.
    • Sodium silicate as corrosion inhibitor and sequestrant is not covered because no read source describes it.
    • The Standard Methods 4500-SiO₂ detection limit was not read; the ISO 16264 range stands in.
    • The ICP-MS interference at mass 28 and the reasons silicon is absent from EPA 200.8 were not read.
    • Textbook citations (MWH chapters 9 and 17) are from memory of the chapters.
    • The magnesium silicate scale and anion exchange stoichiometries are written here from the mechanisms the review describes; it prints neither equation.
    • The second dissociation constant of silicic acid was not read, so no pK₂ is quoted.

    Sources

    Park Y.-M., Yeon K.-M., Park C.-h., Silica treatment technologies in reverse osmosis for industrial desalination: a review, Environmental Engineering Research 25(6), 819 to 829 (2020)
    Australian Drinking Water Guidelines (NHMRC), Part 5, physical and chemical characteristics: Silicon and silica (online, read 2026-09-05)
    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)
    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
    Abu Dhabi Specification ADS 23/2017, Environmental Specifications for Land-Based Liquid Discharges to the Marine Environment (Environment Agency Abu Dhabi), Table 1
    ZDHC Wastewater Guidelines Version 2.1 (November 2022), conventional parameters, anions and metals tables and sludge Table 4A
    WHO GDWQ 4th ed. with addenda (2022), chapter 12 chemical fact sheets on the WHO fact sheet path (aluminium sheet read; no silica sheet exists at that path)
    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)
    US EPA Method 200.8, Revision 5.4 (1994), Determination of trace elements in waters and wastes by ICP-MS, Table 1 (instrument detection limits) and Table 2 (molecular ion interferences)
    ISO 11885:2007, Water quality. Determination of selected elements by inductively coupled plasma optical emission spectrometry (ICP-OES)
    ISO 16264:2002, Water quality. Determination of soluble silicates by flow analysis (FIA and CFA) and photometric detection
    Standard Methods (online edition), 4500-SiO2 Silica (C. molybdosilicate method)
    PubChem element summary for silicon; estimated oceanic abundance 2.2 mg/L (PUG View, reference 5, Jefferson Lab)
    The Element Book, layer 1 entry for silicon (data/elements/Si.json and data/reference/text/Si.json)
    Crittenden, J. C. et al., MWH's Water Treatment: Principles and Design, 3rd ed. (Wiley, 2012), chapter 9 (coagulant aids) and chapter 17 (reverse osmosis scaling)
    Wang C. T., Chou W. L., Chen L. S., Chang S. Y., Silica particles settling characteristics and removal performances of oxide chemical mechanical polishing wastewater treated by electrocoagulation technology, Journal of Hazardous Materials 161(1), 344 to 350 (2009), doi 10.1016/j.jhazmat.2008.03.099 (abstract)
    Setiawan F. A., Rahayuningsih E., Petrus H. T. B. M., Nurpratama M. I., Kinetics of silica precipitation in geothermal brine with seeds addition: minimizing silica scaling in a cold re-injection system, Geothermal Energy 7 (2019), doi 10.1186/s40517-019-0138-3 (abstract)
    Liao Z., Gu Z., Schulz M. C., Davis J. R., Baygents J. C., Farrell J., Treatment of cooling tower blowdown water containing silica, calcium and magnesium by electrocoagulation, Water Science and Technology 60(9), 2345 to 2352 (2009), doi 10.2166/wst.2009.675 (abstract)
    Kawakita H., Morisada S., Ohto K., Germanium recovery using ion-exchange membrane and solvent extraction, Journal of Ion Exchange 25(4), 88 to 92 (2014), doi 10.5182/jaie.25.88 (abstract)

    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.