Toward electrochemical synthesis of cement-An electrolyzer-based process for decarbonating CaCO<sub>3</sub> while producing useful gas streams.

Ellis, Leah D; Badel, Andres F; Chiang, Miki L; Park, Richard J-Y; Chiang, Yet-Ming · Proc Natl Acad Sci U S A · 2020

basic_science · Level V

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Abstract

Cement production is currently the largest single industrial emitter of CO<sub>2</sub>, accounting for ∼8% (2.8 Gtons/y) of global CO<sub>2</sub> emissions. Deep decarbonization of cement manufacturing will require remediation of both the CO<sub>2</sub> emissions due to the decomposition of CaCO<sub>3</sub> to CaO and that due to combustion of fossil fuels (primarily coal) in calcining (∼900 °C) and sintering (∼1,450 °C). Here, we demonstrate an electrochemical process that uses neutral water electrolysis to produce a pH gradient in which CaCO<sub>3</sub> is decarbonated at low pH and Ca(OH)<sub>2</sub> is precipitated at high pH, concurrently producing a high-purity O<sub>2</sub>/CO<sub>2</sub> gas mixture (1:2 molar ratio at stoichiometric operation) at the anode and H<sub>2</sub> at the cathode. We show that the solid Ca(OH)<sub>2</sub> product readily decomposes and reacts with SiO<sub>2</sub> to form alite, the majority cementitious phase in Portland cement. Electrochemical calcination produces concentrated gas streams from which CO<sub>2</sub> may be readily separated and sequestered, H<sub>2</sub> and/or O<sub>2</sub> may be used to generate electric power via fuel cells or combustors, O<sub>2</sub> may be used as a component of oxyfuel in the cement kiln to improve efficiency and lower CO<sub>2</sub> emissions, or the output gases may be used for other value-added processes such as liquid fuel production. Analysis shows that if the hydrogen produced by the reactor were combusted to heat the high-temperature kiln, the electrochemical cement process could be powered solely by renewable electricity.