Robbe Bryssinck, Gregory James Smith, Colin O'Modhrain, Tom Van Assche, Georgi Trenchev and Annemie Bogaerts
{"title":"Performance of a gliding arc plasmatron pilot reactor with an integrated carbon bed and recirculation for upscaled CO2 conversion†","authors":"Robbe Bryssinck, Gregory James Smith, Colin O'Modhrain, Tom Van Assche, Georgi Trenchev and Annemie Bogaerts","doi":"10.1039/D5RE00190K","DOIUrl":null,"url":null,"abstract":"<p >In this work, we investigated the performance of a multi-reactor gliding arc plasmatron (MRGAP) pilot reactor with an integrated carbon bed and recirculation. Experimentally, we varied the following parameters: carbon bed position, total flow rate, recirculation and a semi-continuous feeding system. The optimum operating conditions were found to be with the carbon bed located closest to the reactor outlets (35 mm) at a flow rate of 50 L min<small><sup>−1</sup></small> with a semi-continuous carbon feed. Under these conditions, we obtain a maximum CO<small><sub>2</sub></small> conversion of 20%, corresponding to a conversion rate of 1068 g h<small><sup>−1</sup></small> and a CO concentration of 33 vol% at the outlet. The plug-power based energy cost (EC) for these optimum conditions was 5.8 MWh t<small><sub>CO</sub></small><small><sup>−1</sup></small> (1.2 MJ mol<small><sub>CO<small><sub>2</sub></small></sub></small><small><sup>−1</sup></small>). When implementing a gas recirculation stage, the CO<small><sub>2</sub></small> conversion increases from 10.3% to 12.7%, but the EC rises from 10.9 MWh t<small><sub>CO</sub></small><small><sup>−1</sup></small> to 13.7 MWh t<small><sub>CO</sub></small><small><sup>−1</sup></small>. To complement the experimental work, we also developed a 2D model of the post-plasma chamber, coupled to a simple model for the plasma reactor. The model enables further insights into the effect of the carbon bed position and temperature on the performance, and confirms that when the carbon bed is positioned closer to the inlets, the performance increases. Both experimental and modelling results indicate that the integration of a carbon bed into an industrial scale plasma reactor is viable and can improve both the CO<small><sub>2</sub></small> conversion and energy metrics.</p>","PeriodicalId":101,"journal":{"name":"Reaction Chemistry & Engineering","volume":" 8","pages":" 1910-1923"},"PeriodicalIF":3.1000,"publicationDate":"2025-05-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Reaction Chemistry & Engineering","FirstCategoryId":"92","ListUrlMain":"https://pubs.rsc.org/en/content/articlelanding/2025/re/d5re00190k","RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
Abstract
In this work, we investigated the performance of a multi-reactor gliding arc plasmatron (MRGAP) pilot reactor with an integrated carbon bed and recirculation. Experimentally, we varied the following parameters: carbon bed position, total flow rate, recirculation and a semi-continuous feeding system. The optimum operating conditions were found to be with the carbon bed located closest to the reactor outlets (35 mm) at a flow rate of 50 L min−1 with a semi-continuous carbon feed. Under these conditions, we obtain a maximum CO2 conversion of 20%, corresponding to a conversion rate of 1068 g h−1 and a CO concentration of 33 vol% at the outlet. The plug-power based energy cost (EC) for these optimum conditions was 5.8 MWh tCO−1 (1.2 MJ molCO2−1). When implementing a gas recirculation stage, the CO2 conversion increases from 10.3% to 12.7%, but the EC rises from 10.9 MWh tCO−1 to 13.7 MWh tCO−1. To complement the experimental work, we also developed a 2D model of the post-plasma chamber, coupled to a simple model for the plasma reactor. The model enables further insights into the effect of the carbon bed position and temperature on the performance, and confirms that when the carbon bed is positioned closer to the inlets, the performance increases. Both experimental and modelling results indicate that the integration of a carbon bed into an industrial scale plasma reactor is viable and can improve both the CO2 conversion and energy metrics.
期刊介绍:
Reaction Chemistry & Engineering is a new journal reporting cutting edge research into all aspects of making molecules for the benefit of fundamental research, applied processes and wider society.
From fundamental, molecular-level chemistry to large scale chemical production, Reaction Chemistry & Engineering brings together communities of chemists and chemical engineers working to ensure the crucial role of reaction chemistry in today’s world.