Biomass fly-ash derived Li4SiO4 solid for pilot-scale CO2 capture, Part I: Modelling for a waste to capture CO2 process

This work presents a new modelled system of a biomass-based lithium orthosilicate solid adsorbent derived from industrial biomass fly-ash used to capture CO 2 from power plant flue gas emissions. The model includes pre-treatment of biomass fly-ash, the synthesis of adsorbent, which utilizes fly-ash as the silicone source and a laboratory produced lithium source, the adsorption of CO 2 from flue gas, and regeneration of adsorbent. The study compares the results from pre-treated and non-pre-treated biomass fly-ash, with benchmark CO 2 capture rates of 87 % and 89.7 %, respectively and a maximum CO 2 capture rate of 93.23 %. Key insights from the scenarios considered in this work show that an increased CO 2 flue gas composition requires higher adsorbent mass and the most effective flue gas volume to adsorbent mass ratio between 3.7–4.1; additionally, higher regeneration temperatures result in improved CO 2 capture while pre-treatment of fly-ash does not impact regeneration kinetics. Energy analysis show that the pre-treated fly-ash adsorbent is more efficient than the non-pretreated adsorbent but is not superior to amine-based post-combustion carbon capture. If effective heat integration were to be incorporated for the pre-treated and non-pre-treated adsorption processes, energy consumption could be reduced by 54 % and 85 % compared to amine-based capture, respectively. Cost analysis indicated that by incorporating a recycle stream for pre-treatment wastewater and altering the acid to solid ratio during pre-treatment acid wash, process costs may be reduced over 20 % making this a feasible alternative carbon capture process. • A CO2 capture model that uses a biomass-based adsorbent from fly-ash is presented. • Model includes pre-treatment section, adsorption of CO2 and regeneration of Li4SiO4. • Model’s performance under changes in key process parameters was investigated. • Energy and cost analyses were made and compared to MEA-based capture plant.

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Publication Details

Journal
Process Safety and Environmental Protection
Published
2024-12-27
DOI
https://doi.org/10.1016/j.cherd.2024.12.036
Citations
5
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
1.06

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article

Biomass fly-ash derived Li4SiO4 solid for pilot-scale CO2 capture, Part I: Modelling for a waste to capture CO2 process

Luis Ricardez‐Sandoval, Samantha A Usas
5 citations
Process Safety and Environmental Protection
Extraction and Separation Processes
1.06
article

Biomass fly-ash derived Li4SiO4 solid for pilot-scale CO2 capture, Part I: Modelling for a waste to capture CO2 process

Luis Ricardez‐Sandoval, Samantha A Usas
article en
5 citations

Abstract

This work presents a new modelled system of a biomass-based lithium orthosilicate solid adsorbent derived from industrial biomass fly-ash used to capture CO 2 from power plant flue gas emissions. The model includes pre-treatment of biomass fly-ash, the synthesis of adsorbent, which utilizes fly-ash as the silicone source and a laboratory produced lithium source, the adsorption of CO 2 from flue gas, and regeneration of adsorbent. The study compares the results from pre-treated and non-pre-treated biomass fly-ash, with benchmark CO 2 capture rates of 87 % and 89.7 %, respectively and a maximum CO 2 capture rate of 93.23 %. Key insights from the scenarios considered in this work show that an increased CO 2 flue gas composition requires higher adsorbent mass and the most effective flue gas volume to adsorbent mass ratio between 3.7–4.1; additionally, higher regeneration temperatures result in improved CO 2 capture while pre-treatment of fly-ash does not impact regeneration kinetics. Energy analysis show that the pre-treated fly-ash adsorbent is more efficient than the non-pretreated adsorbent but is not superior to amine-based post-combustion carbon capture. If effective heat integration were to be incorporated for the pre-treated and non-pre-treated adsorption processes, energy consumption could be reduced by 54 % and 85 % compared to amine-based capture, respectively. Cost analysis indicated that by incorporating a recycle stream for pre-treatment wastewater and altering the acid to solid ratio during pre-treatment acid wash, process costs may be reduced over 20 % making this a feasible alternative carbon capture process. • A CO2 capture model that uses a biomass-based adsorbent from fly-ash is presented. • Model includes pre-treatment section, adsorption of CO2 and regeneration of Li4SiO4. • Model’s performance under changes in key process parameters was investigated. • Energy and cost analyses were made and compared to MEA-based capture plant.

Process Safety and Environmental ProtectionVol. 214
University of Waterloo (CA)
Natural Sciences and Engineering Research Council of Canada
Openalex Percentile: Top 25%
Extraction and Separation Processes
1.06
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