Calcium CarbonateDecomposition Coupled with In SituConversion of CO<sub>2</sub> into Syngas: Industrial Scenario Analysisfor Carbon Capture and Clinker Production

CaCO<sub>3</sub> calcination is closely associated with the production of essential materials. However, the manufacturing processes are characterized by high temperatures and intense CO<sub>2</sub> emissions. Herein, we proposed a novel technology called CaCO<sub>3</sub> bireforming of CH<sub>4</sub> (CaBRM), which converted CaCO<sub>3</sub> directly into CaO and syngas through the combined steam and dry reforming of CH<sub>4</sub> (BRM). First, thermodynamic analysis and temperature-programmed calcination experiments were conducted to validate the feasibility of CaBRM technology. Then, two industrial scenarios were established using Aspen Plus. In Scenario 1, implementing an integrated calcium looping (CaL) and BRM process for CO<sub>2</sub> capture and utilization (CCU) reduced energy consumption, carbon emissions, and costs by 43, 28, and 27%, respectively, compared to conventional CCU. In Scenario 2, CaBRM technology enabled low-carbon clinker production with reduced energy consumption (2.711 MJ/kgClinker), lower carbon footprint (0.157 kgCO<sub>2</sub>e/kgClinker), decreased production costs (126.38 USD/tClinker), and syngas coproduction. Thus, the CaBRM technology achieved energy savings, emission reduction, and in situ CO<sub>2</sub> conversion, making it a promising option for carbon mitigation in the carbonate-related industry.

Publication Details

Journal
Figshare
Published
2025-01-22
DOI
https://doi.org/10.1021/acs.iecr.4c02692.s001
Primary Topic
Mycorrhizal Fungi and Plant Interactions
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article
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Calcium CarbonateDecomposition Coupled with In SituConversion of CO2 into Syngas: Industrial Scenario Analysisfor Carbon Capture and Clinker Production

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Mycorrhizal Fungi and Plant Interactions
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Calcium CarbonateDecomposition Coupled with In SituConversion of CO2 into Syngas: Industrial Scenario Analysisfor Carbon Capture and Clinker Production

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Abstract

CaCO<sub>3</sub> calcination is closely associated with the production of essential materials. However, the manufacturing processes are characterized by high temperatures and intense CO<sub>2</sub> emissions. Herein, we proposed a novel technology called CaCO<sub>3</sub> bireforming of CH<sub>4</sub> (CaBRM), which converted CaCO<sub>3</sub> directly into CaO and syngas through the combined steam and dry reforming of CH<sub>4</sub> (BRM). First, thermodynamic analysis and temperature-programmed calcination experiments were conducted to validate the feasibility of CaBRM technology. Then, two industrial scenarios were established using Aspen Plus. In Scenario 1, implementing an integrated calcium looping (CaL) and BRM process for CO<sub>2</sub> capture and utilization (CCU) reduced energy consumption, carbon emissions, and costs by 43, 28, and 27%, respectively, compared to conventional CCU. In Scenario 2, CaBRM technology enabled low-carbon clinker production with reduced energy consumption (2.711 MJ/kgClinker), lower carbon footprint (0.157 kgCO<sub>2</sub>e/kgClinker), decreased production costs (126.38 USD/tClinker), and syngas coproduction. Thus, the CaBRM technology achieved energy savings, emission reduction, and in situ CO<sub>2</sub> conversion, making it a promising option for carbon mitigation in the carbonate-related industry.

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Calcium CarbonateDecomposition Coupled with In SituConversion of CO<sub>2</sub> into Syngas: Industrial Scenario Analysisfor Carbon Capture and Clinker Production · Figshare (2025) | TGRS Research Map | TGRS