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Curbing the greenhouse effect by carbon dioxide adsorption with Zeolite 13X
The removal of carbon dioxide (CO₂) from industrial emissions has become essential in the fight against climate change. In this study, we employed Zeolite 13X for the capture and recovery of CO₂ in a flow through system where the adsorbent was subjected to five adsorption-desorption cycles. The infl...
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Published in: | AIChE journal 2007-12, Vol.53 (12), p.3137-3143 |
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Main Authors: | , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | The removal of carbon dioxide (CO₂) from industrial emissions has become essential in the fight against climate change. In this study, we employed Zeolite 13X for the capture and recovery of CO₂ in a flow through system where the adsorbent was subjected to five adsorption-desorption cycles. The influent stream contained 1.5% CO₂ at standard conditions. The adsorbent bed was 1 in. in length and 1 in. 3/8 in dia., and was packed with 10 g of the zeolite. Temperature swing adsorption (TSA) was employed as the regeneration method through heating to approximately 135 °C with helium as the purge gas. The adsorbent capacity at 90% saturation was found to decrease from 78 to 60gCO₂/kgZeolite₁₃X after the fifth cycle. The CO₂ capture ratio or the mass of CO₂ adsorbed to the total mass that entered the system decreased from 63% to only 61% after the fifth cycle. The CO₂ recovery efficiency ranged from 82 to 93% during desorption, and the CO₂ relative recovery, i.e., CO₂ desorbed for the nth cycle to CO₂ adsorbed for the first cycle, ranged from 88 to 68%. The service life of the adsorbent was determined to be equal to eleven cycles at a useful capacity of 40gCO₂/kgZeolite₁₃X. © 2007 American Institute of Chemical Engineers AIChE J, 2007 |
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ISSN: | 0001-1541 1547-5905 |
DOI: | 10.1002/aic.11318 |