Schikorr reaction

Schikorr reaction
iron(II) hydroxide, Fe(OH)2, the start-reagent of the Schikorr reaction.
Magnified crystals of iron(II,III) oxide (Fe3O4), the end-product of the Schikorr reaction along with hydrogen gas.

The Schikorr reaction formally describes the conversion of the iron(II) hydroxide (Fe(OH)2) into iron(II,III) oxide (Fe3O4).

The bases of this transformation reaction were first studied by Gerhard Schikorr, a German specialist of iron corrosion, in his early works (~1928-1933) on iron(II) and iron(III) hydroxides. The global reaction that Schikorr proposed to explain his observations onto the iron hydroxides conversion, and which later received his name, can be written as follows:

3 Fe(OH)2 → Fe3O4 + H2 + 2 H2O

Contents

Reaction mechanism

The Schikorr reaction involves two distinct processes:

  • the anaerobic oxidation of two Fe(II) (Fe2+) into Fe(III) (Fe3+) by the protons of water. The reduction of two water protons is accompanied by the production of molecular hydrogen (H2), and;
  • the loss of two water molecules from the iron(II) and iron(III) hydroxides giving rise to its dehydration and to the formation of a thermodynamically more stable phase iron(II,III) oxide.

The global reaction can thus be decomposed in half redox reactions as follows:

2 (Fe2+ → Fe3+ + e) (oxidation of 2 iron(II) ions)
2 (H2O + e → ½ H2 + OH) (reduction of 2 water protons)

to give:

2 Fe2+ + 2 H2O → 2 Fe3+ + H2 + 2 OH

Adding to this reaction one intact iron(II) ion for each two oxidized iron(II) ions leads to:

3 Fe2+ + 2 H2O → Fe2+ + 2 Fe3+ + H2 + 2 OH

Electroneutrality requires the iron cations on both sides of the equation to be counter-balanced by 6 hydroxyl anions (OH):

3 Fe2+ + 6 OH + 2 H2O → Fe2+ + 2 Fe3+ + H2 + 8 OH
3 Fe(OH)2 + 2 H2O → Fe(OH)2 + 2 Fe(OH)3 + H2

For completing the main reaction, two companion reactions have still to be taken into account:

The autoprotolysis of the hydroxyl anions; a proton exchange between two OH, like in a classical acid-base reaction:

OH + OH → O2– + H2O
acid 1 + base 2 → base 1 + acid 2, or also,
2 OH → O2– + H2O

it is then possible to reorganize the global reaction as:

3 Fe(OH)2 + 2 H2O → (FeO + H2O) + (Fe2O3 + 3 H2O) + H2
3 Fe(OH)2 + 2 H2O → FeO + Fe2O3 + 4 H2O + H2
3 Fe(OH)2 → FeO + Fe2O3 + 2 H2O + H2

Considering then the formation reaction of iron(II,III) oxide:

Fe(II)O + Fe(III)2O3 → Fe3O4

it is possible to write the balanced global reaction:

3 Fe(OH)2 → (FeO·Fe2O3) + 2 H2O + H2

in its final form, known as the Schikorr reaction:

3 Fe(OH)2 → Fe3O4 + 2 H2O + H2

Occurrences

The Schikorr reaction can occur in the process of anaerobic corrosion of iron and carbon steel in various conditions.

Anaerobic corrosion of metallic iron to give iron(II) hydroxide and hydrogen:

3 (Fe + 2 H2O → Fe(OH)2 + H2)

followed by the Schikorr reaction:

3 Fe(OH)2 → Fe3O4 + 2 H2O + H2

give the following global reaction:

3 Fe + 6 H2O → Fe3O4 + 2 H2O + 4 H2
3 Fe + 4 H2O → Fe3O4 + 4 H2

At low temperature, the anaerobic corrosion of iron can give rise to the formation of "green rust" (fougerite) an unstable layered double hydroxide (LDH). In function of the geochemical conditions prevailing in the environment of the corroding steel, iron(II) hydroxide and green rust can progressively transform in iron(II,III) oxide, or if bicarbonate ions are present in solution, they can also evolve towards more stable carbonate phases such as iron carbonate (FeCO3), or iron(II) hydroxycarbonate (Fe2(OH)2(CO3), chukanovite) isomorphic to copper(II) hydroxycarbonate (Cu2(OH)2(CO3), malachite) in the copper system.

Application fields

Anaerobic oxidation of iron and steel commonly finds place in oxygen-depleted environments, such as in permanently water-saturated soils, peat bogs or wetlands in which archaeological iron artefacts are often found.

Anaerobic oxidation of carbon steel of canisters and overpacks is also expected to occur in deep geological formations in which high-level radioactive waste (HLW) and spent fuels (SF) should be ultimately disposed. Nowadays, in the frame of the corrosion studies related to HLW disposal, anaerobic corrosion of steel is receiving a renewed and continued attention. Indeed, it is essential to understand this process to guarantee the total containment of HLW waste in an engineered barrier during the first centuries or millennia when the radiotoxicity of the waste is high and when it emits a significant quantity of heat.

The question is also relevant for the corrosion of the reinforcement bars (rebars) in concrete (Aligizaki et al., 2000). This deals then with the service life of concrete structures, amongst others the near-surface vaults intended for hosting low-level radioactive waste.

Hydrogen evolution

The slow but continuous production of hydrogen in deep low-permeability argillaceous formations could represent a problem for the long-term disposal of radioactive waste (Ortiz et al., 2001; Nagra, 2008; recent Nagra NTB reports). Indeed, a gas pressure build-up could occur if the rate of hydrogen production by the anaerobic corrosion of carbon-steel and by the subsequent transformation of green rust into magnetite should exceed the rate of diffusion of dissolved H2 in the pore water of the formation. The question is presently the object of many studies (King, 2008; King and Kolar, 2009; Nagra Technical Reports 2000–2009) in the countries (Belgium, Switzerland, France, Canada) envisaging the option of disposal in clay formation.

Hydrogen embrittlement of steel alloys

When nascent hydrogen is produced by anaerobic corrosion of iron by the protons of water, the atomic hydrogen can diffuse into the metal crystal lattice because of the existing concentration gradient. After diffusion, hydrogen atoms can recombine into molecular hydrogen giving rise to the formation of high-pressure micro-bubbles of H2 in the metallic lattice. The trends to expansion of H2 bubbles and the resulting tensile stress can generate cracks in the metallic alloys sensitive to this effect also known as hydrogen embrittlement. Several recent studies (Turnbull, 2009; King, 2008; King and Kolar, 2009) address this question in the frame of the radioactive waste disposal in Switzerland and Canada.

See also

3 Fe2SiO4 + 2 H2O → 2 Fe3O4 + 3 SiO2 + 3 H2

References

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Beverskog, B.; I. Puigdomenech (1996-12). "Revised Pourbaix diagrams for iron at 25-300 °C". Corrosion Science 38 (12): 2121–2135. doi:10.1016/S0010-938X(96)00067-4. ISSN 0010-938X. http://www.sciencedirect.com/science/article/B6TWS-3VSNG79-6/2/94cd01f8cff318412011d838c7d7bbb8. Retrieved 2010-08-01. 

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King, F.; M. Kolar (2009). Theory manual for the steel corrosion model version 1.0. NWMO TR-2009-07 March 2009. 

Landolt, D.; A. Davenport, J. Payer, D. Shoesmith (2009). "A review of materials and corrosion issues regarding canisters for disposal of spent fuel and high-level waste in Opalinus Clay. Nagra Technical Report NTB 09-02.". http://www.nagra.ch/g3.cms/s_page/83220/s_name/shopproductdetail1/s_element/142590/s_level/10190/s_product/20902/searchkey/Corrosion. Retrieved 2010-08-01. 

Nagra (2008). "Effects of post-disposal gas generation in a repository for low- and intermediate-level waste sited in the Opalinus Clay of Northern Switzerland. Nagra Technical Report NTB 08-07". http://www.nagra.ch/g3.cms/s_page/83220/s_name/shopproductdetail1/s_element/142590/s_level/10190/s_product/20807/searchkey/Corrosion. Retrieved 2010-08-01. 

Odziemkowski, M. S.; T. T. Schuhmacher, R. W. Gillham, E. J. Reardon. "Mechanism of oxide film formation on iron in simulating groundwater solutions: Raman spectroscopic studies". Corrosion Science 40 (2-3): 371–389. doi:10.1016/S0010-938X(97)00141-8. ISSN 0010-938X. 

Ortiz, L.; G. Volckaert, D. Mallants (2002-05). "Gas generation and migration in Boom Clay, a potential host rock formation for nuclear waste storage". Engineering Geology 64 (2-3): 287–296. doi:10.1016/S0013-7952(01)00107-7. ISSN 0013-7952. 

Regazzoni, A. E.; G. A. Urrutia, M. A. Blesa, A. J. G. Maroto (1981). "Some observations on the composition and morphology of synthetic magnetites obtained by different routes". Journal of Inorganic and Nuclear Chemistry 43 (7): 1489–1493. doi:10.1016/0022-1902(81)80322-3. ISSN 0022-1902. http://www.sciencedirect.com/science/article/B758S-48M3K71-1V2/2/637bf8f35370dccefc43992cf5783961. Retrieved 2010-08-01. 

Deiss, E.; G. Schikorr (1928). "Über das ferrohydroxyd (eisen-2-hydroxyd)". Zeitschrift für Anorganische und Allgemeine Chemie 172 (1): 32–42. doi:10.1002/zaac.19281720103. 

Schikorr, Gerhard (1933). "The iron (II) hydroxide and a ferromagnetic iron (III) hydroxide". Zeitschrift für Anorganische und Allgemeine Chemie 212 (1): 33–39. doi:10.1002/zaac.19332120105. 

Schikorr, Gerhard (1933). "Über eisen(II)-hydroxyd und ein ferromagnetisches eisen(III)-hydroxyd". Zeitschrift für Anorganische und Allgemeine Chemie 212 (1): 33–39. doi:10.1002/zaac.19332120105. 

Schikorr, Gerhard (1963). "Über den mechanismus des atmosphärischen rostens des eisens". Werkstoffe und Korrosion 14 (2): 69–80. doi:10.1002/maco.19630140203. 

Smart, N.R.; D.J. Blackwood, L. Werme (2002). "Anaerobic corrosion of carbon steel and cast iron in artificial groundwaters: Part 1, Electrochemical aspects". http://www.onepetro.org/mslib/servlet/onepetropreview?id=NACE-02070547&soc=NACE&speAppNameCookie=ONEPETRO. Retrieved 2010-08-01. 

Turnbull, Alan (2009). "A review of the possible effects of hydrogen on lifetime of carbon steel nuclear waste canisters. Nagra Technical Report NTB 09-04.". http://www.nagra.ch/g3.cms/s_page/83220/s_name/shopproductdetail1/s_element/142590/s_level/10190/s_product/20904/searchkey/Corrosion. Retrieved 2010-08-01. 

Webb, S.L.; G. Bohnsack. "The kinetics of the Schikorr reaction on steel surfaces at low temperatures". http://md1.csa.com/partners/viewrecord.php?requester=gs&collection=TRD&recid=890664CO&q=Schikorr+reaction&uid=789698683&setcookie=yes. Retrieved 2010-08-01. 

External links

For detailed reports on iron corrosion issues related to high-level waste disposal, see the following links:


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