Negative CO2 emissions through iG-CLC of pinus residue in a continuous unit of 0.5 kWth using a natural Mn-based oxygen carrier

The use of renewable fuels, as biomass, in the chemical looping combustion process becomes an attractive solution to bioenergy technology with CO 2 capture (BECCS). In this work, a manganese ore from Brazil (MnT1000) was evaluated as an oxygen carrier to promote the conversion of a pine residue biomass by the in-situ Gasification-Chemical Looping Combustion ( i G-CLC) technology in a 0.5 kW th continuous experimental unit installed at ICB-CSIC. The main parameters studied were the influence of fuel reactor temperature, air excess, and oxygen-to-biomass ratio on the performance of the MnT1000 evaluating CO 2 capture efficiency and total oxygen demand. Under all experimental conditions, CO 2 composition was higher than 84% at the fuel reactor outlet gas on a dry N 2 -free basis. The unburned gases such as CH 4 , CO and H 2 were present in low concentration, attributed to the high reactivity that MnT1000 has with H 2 , CO and CH 4 . In general, higher temperatures, higher oxygen excess ratio and lower oxygen-to-biomass ratio reduced the total oxygen demand, with no great influence on CO 2 capture efficiency. Most of the experiments showed capture efficiency above 90%, and a total oxygen demand in between 5.9 and 13.7% for the experimental conditions studied with low specific solid inventories (760 – 833 kg MW −1 ). The amount of tar quantified in this study was low, corresponding to a total of 1.32 g Nm −3 , composed mainly of naphthalene and phenanthrene. In all experimental conditions, MnT1000 showed promising behavior, its reactivity remained high and constant throughout whole operation and no agglomeration problems were observed. • MnT1000 has high reactivity with H 2 , CO, and CH 4 . • MnT1000 kept its integrity and reactivity after 36 h of continuous operation. • i G-CLC process with MnT1000 showed CO 2 capture efficiency higher than 87%. • Experiments highlighted low tar formation at 900 °C. • With low specific solids inventory, low oxygen demand and low tars were achieved.

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Publication Details

Journal
Biomass and Bioenergy
Published
2025-02-13
DOI
https://doi.org/10.1016/j.biombioe.2025.107681
Citations
2
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
1.35

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article

Negative CO2 emissions through iG-CLC of pinus residue in a continuous unit of 0.5 kWth using a natural Mn-based oxygen carrier

Juan Adánez, Dulce Maria de Araújo Melo, Renata Martins Braga, Gislane Pinho de Oliveira et al.
2 citations
Biomass and Bioenergy
Chemical Looping and Thermochemical Processes
1.35
article

Negative CO2 emissions through iG-CLC of pinus residue in a continuous unit of 0.5 kWth using a natural Mn-based oxygen carrier

Juan Adánez, Dulce Maria de Araújo Melo, Renata Martins Braga, Gislane Pinho de Oliveira, Iñaki Adánez-Rubio, TIAGO ROBERTO DA COSTA
article en
2 citations

Abstract

The use of renewable fuels, as biomass, in the chemical looping combustion process becomes an attractive solution to bioenergy technology with CO 2 capture (BECCS). In this work, a manganese ore from Brazil (MnT1000) was evaluated as an oxygen carrier to promote the conversion of a pine residue biomass by the in-situ Gasification-Chemical Looping Combustion ( i G-CLC) technology in a 0.5 kW th continuous experimental unit installed at ICB-CSIC. The main parameters studied were the influence of fuel reactor temperature, air excess, and oxygen-to-biomass ratio on the performance of the MnT1000 evaluating CO 2 capture efficiency and total oxygen demand. Under all experimental conditions, CO 2 composition was higher than 84% at the fuel reactor outlet gas on a dry N 2 -free basis. The unburned gases such as CH 4 , CO and H 2 were present in low concentration, attributed to the high reactivity that MnT1000 has with H 2 , CO and CH 4 . In general, higher temperatures, higher oxygen excess ratio and lower oxygen-to-biomass ratio reduced the total oxygen demand, with no great influence on CO 2 capture efficiency. Most of the experiments showed capture efficiency above 90%, and a total oxygen demand in between 5.9 and 13.7% for the experimental conditions studied with low specific solid inventories (760 – 833 kg MW −1 ). The amount of tar quantified in this study was low, corresponding to a total of 1.32 g Nm −3 , composed mainly of naphthalene and phenanthrene. In all experimental conditions, MnT1000 showed promising behavior, its reactivity remained high and constant throughout whole operation and no agglomeration problems were observed. • MnT1000 has high reactivity with H 2 , CO, and CH 4 . • MnT1000 kept its integrity and reactivity after 36 h of continuous operation. • i G-CLC process with MnT1000 showed CO 2 capture efficiency higher than 87%. • Experiments highlighted low tar formation at 900 °C. • With low specific solids inventory, low oxygen demand and low tars were achieved.

Biomass and BioenergyVol. 195
Universidade Federal do Rio Grande do Norte (BR), Faculdade de Medicina de Jundiaí (BR), Instituto de Carboquímica (ES), Universidade Federal do Maranhão (BR)
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior, Conselho Nacional de Desenvolvimento Científico e Tecnológico, Ministerio de Ciencia e Innovación
Openalex Percentile: Top 22%
Chemical Looping and Thermochemical Processes
1.35
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