Techno-economic and life cycle environmental assessments of CO2 utilization for value-added precipitated calcium carbonate and ammonium sulfate fertilizer co-production

An advanced CO 2 mineralization technology using Flue Gas Desulfurization (FGD) byproduct gypsum, which coproduces value-added precipitated calcium carbonate (precipitated CaCO 3 , PCC) and ammonium sulfate [(NH 4 ) 2 SO 4 , AS] fertilizer, is being developed to address the technical challenges of achieving simultaneous CO 2 capture and utilization, high CO 2 and calcium conversion, and enhanced energy efficiency. This study aimed to conduct a techno-economic analysis (TEA) and a life cycle assessment (LCA) for this technology. In the TEA, mass and energy balances for CO 2 mineralization integrated with a power plant to utilize all FGD gypsum and approximately 51,000 tonne/year of CO 2 in flue gas were developed through modeling. Major equipment was selected and sized, followed by capital and operating cost analyses. Energy efficiency was improved through the integrated use of both low-grade steam and vacuum from the power plant steam cycle. TEA results revealed that this process was profitable, with a levelized net profit of $328.4 per tonne of CO 2 utilized. The LCA was performed as a cradle-to-gate study for comparative assessments of global warming potential (GWP) and other environmental impacts between the CO 2 mineralization system (i.e., Proposed Production System or PPS) and the conventional processes (i.e., Comparison Production System or CPS). The PPS resulted in a GWP impact of 0.85 kg CO 2 -Eq per 1 kg of primary PCC production and 1.32 kg of byproduct AS production, approximately 64 % lower than that of the CPS. The LCA results for other environmental impacts also consistently showed impacts 35–88 % lower for the PPS compared to the CPS. • A process for simultaneous CO 2 capture and mineralization with FGD gypsum is developed. • Energy use was reduced through process intensification and integration with power plants. • CO 2 mineralization with FGD gypsum generates a net profit of $328.4 per tonne of CO 2 . • The Global Warming Potential impact is 64 % lower than conventional processes. • Equipment and operations with major economic or environmental impacts are identified.

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Publication Details

Journal
Journal of CO2 Utilization
Published
2024-12-01
DOI
https://doi.org/10.1016/j.jcou.2024.102992
Citations
8
Primary Topic
Calcium Carbonate Crystallization and Inhibition
Type
article
Field-Weighted Citation Impact
1.39

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article

Techno-economic and life cycle environmental assessments of CO2 utilization for value-added precipitated calcium carbonate and ammonium sulfate fertilizer co-production

Partha Saha, Feyza Kazanç, Yongqi Lu, Peng Zhang
8 citations
Journal of CO2 Utilization
Calcium Carbonate Crystallization and Inhibition
1.39
article

Techno-economic and life cycle environmental assessments of CO2 utilization for value-added precipitated calcium carbonate and ammonium sulfate fertilizer co-production

Partha Saha, Feyza Kazanç, Yongqi Lu, Peng Zhang
article en
8 citations

Abstract

An advanced CO 2 mineralization technology using Flue Gas Desulfurization (FGD) byproduct gypsum, which coproduces value-added precipitated calcium carbonate (precipitated CaCO 3 , PCC) and ammonium sulfate [(NH 4 ) 2 SO 4 , AS] fertilizer, is being developed to address the technical challenges of achieving simultaneous CO 2 capture and utilization, high CO 2 and calcium conversion, and enhanced energy efficiency. This study aimed to conduct a techno-economic analysis (TEA) and a life cycle assessment (LCA) for this technology. In the TEA, mass and energy balances for CO 2 mineralization integrated with a power plant to utilize all FGD gypsum and approximately 51,000 tonne/year of CO 2 in flue gas were developed through modeling. Major equipment was selected and sized, followed by capital and operating cost analyses. Energy efficiency was improved through the integrated use of both low-grade steam and vacuum from the power plant steam cycle. TEA results revealed that this process was profitable, with a levelized net profit of $328.4 per tonne of CO 2 utilized. The LCA was performed as a cradle-to-gate study for comparative assessments of global warming potential (GWP) and other environmental impacts between the CO 2 mineralization system (i.e., Proposed Production System or PPS) and the conventional processes (i.e., Comparison Production System or CPS). The PPS resulted in a GWP impact of 0.85 kg CO 2 -Eq per 1 kg of primary PCC production and 1.32 kg of byproduct AS production, approximately 64 % lower than that of the CPS. The LCA results for other environmental impacts also consistently showed impacts 35–88 % lower for the PPS compared to the CPS. • A process for simultaneous CO 2 capture and mineralization with FGD gypsum is developed. • Energy use was reduced through process intensification and integration with power plants. • CO 2 mineralization with FGD gypsum generates a net profit of $328.4 per tonne of CO 2 . • The Global Warming Potential impact is 64 % lower than conventional processes. • Equipment and operations with major economic or environmental impacts are identified.

Journal of CO2 UtilizationVol. 90
Illinois Archaeological Survey (US)
U.S. Department of Energy, National Energy Technology Laboratory
Zero hunger, Responsible consumption and production
Openalex Percentile: Top 20%
Calcium Carbonate Crystallization and Inhibition
1.39
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