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Conceptual evaluation of an integrated CCU technology based on Na-salts pH swing mineral carbonation

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Conceptual evaluation of an integrated CCU technology based on Na-salts pH swing mineral carbonation. / Bagnato, G.; Sanna, A.
In: Journal of CO2 Utilization, Vol. 66, 102286, 31.12.2022.

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Bagnato G, Sanna A. Conceptual evaluation of an integrated CCU technology based on Na-salts pH swing mineral carbonation. Journal of CO2 Utilization. 2022 Dec 31;66:102286. Epub 2022 Oct 27. doi: 10.1016/j.jcou.2022.102286

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@article{71f26511e1b543fa93f95ab7ce822df5,
title = "Conceptual evaluation of an integrated CCU technology based on Na-salts pH swing mineral carbonation",
abstract = "This work proposes an alternative indirect pH swing CO2 Capture and Storage by Mineral Carbonation (CCSM) process in order to decrease the energy intensive salts regeneration. In the proposed process, NaHSO4 is used to extract Mg from the mineral ore, which is then carbonated after a pH swing step. The remaining Na2SO4 is then separated from the carbonation solution taking advantage of its low solubility at temperatures close to 0 °C and then regenerated to NaOH and NaHSO4 in three stages. The integrated process that uses both Mg-rich silicates and inorganic wastes, was experimentally proved, and their energy consumption calculated. The final CO2 sequestration capacity was of 77.4% with enhanced recovery of metals in the pH swing step, which could offset the CCSM by about $50/t CO2. The final regeneration step showed a 55% conversion of Na2CO3 to CaCO3 at 120 °C under 3 bar and the conversion rate could be improved further by optimization. The energy consumption estimation without optimisation indicated that the sodium-based process would require about 19.6 GJ/tCO2, which at this stage of development is larger than the optimised {\AA}bo Akademi process (12-15.5 GJ/tCO2), but considerably lower than the University of Nottingham's process (30 GJ/tCO2).",
keywords = "Sodium salts, CO2 fixation, CCS, Mineral carbonation, Applied energy",
author = "G. Bagnato and A. Sanna",
year = "2022",
month = dec,
day = "31",
doi = "10.1016/j.jcou.2022.102286",
language = "English",
volume = "66",
journal = "Journal of CO2 Utilization",
issn = "2212-9820",
publisher = "Elsevier BV",

}

RIS

TY - JOUR

T1 - Conceptual evaluation of an integrated CCU technology based on Na-salts pH swing mineral carbonation

AU - Bagnato, G.

AU - Sanna, A.

PY - 2022/12/31

Y1 - 2022/12/31

N2 - This work proposes an alternative indirect pH swing CO2 Capture and Storage by Mineral Carbonation (CCSM) process in order to decrease the energy intensive salts regeneration. In the proposed process, NaHSO4 is used to extract Mg from the mineral ore, which is then carbonated after a pH swing step. The remaining Na2SO4 is then separated from the carbonation solution taking advantage of its low solubility at temperatures close to 0 °C and then regenerated to NaOH and NaHSO4 in three stages. The integrated process that uses both Mg-rich silicates and inorganic wastes, was experimentally proved, and their energy consumption calculated. The final CO2 sequestration capacity was of 77.4% with enhanced recovery of metals in the pH swing step, which could offset the CCSM by about $50/t CO2. The final regeneration step showed a 55% conversion of Na2CO3 to CaCO3 at 120 °C under 3 bar and the conversion rate could be improved further by optimization. The energy consumption estimation without optimisation indicated that the sodium-based process would require about 19.6 GJ/tCO2, which at this stage of development is larger than the optimised Åbo Akademi process (12-15.5 GJ/tCO2), but considerably lower than the University of Nottingham's process (30 GJ/tCO2).

AB - This work proposes an alternative indirect pH swing CO2 Capture and Storage by Mineral Carbonation (CCSM) process in order to decrease the energy intensive salts regeneration. In the proposed process, NaHSO4 is used to extract Mg from the mineral ore, which is then carbonated after a pH swing step. The remaining Na2SO4 is then separated from the carbonation solution taking advantage of its low solubility at temperatures close to 0 °C and then regenerated to NaOH and NaHSO4 in three stages. The integrated process that uses both Mg-rich silicates and inorganic wastes, was experimentally proved, and their energy consumption calculated. The final CO2 sequestration capacity was of 77.4% with enhanced recovery of metals in the pH swing step, which could offset the CCSM by about $50/t CO2. The final regeneration step showed a 55% conversion of Na2CO3 to CaCO3 at 120 °C under 3 bar and the conversion rate could be improved further by optimization. The energy consumption estimation without optimisation indicated that the sodium-based process would require about 19.6 GJ/tCO2, which at this stage of development is larger than the optimised Åbo Akademi process (12-15.5 GJ/tCO2), but considerably lower than the University of Nottingham's process (30 GJ/tCO2).

KW - Sodium salts

KW - CO2 fixation

KW - CCS

KW - Mineral carbonation

KW - Applied energy

U2 - 10.1016/j.jcou.2022.102286

DO - 10.1016/j.jcou.2022.102286

M3 - Journal article

VL - 66

JO - Journal of CO2 Utilization

JF - Journal of CO2 Utilization

SN - 2212-9820

M1 - 102286

ER -