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Effects of water vapor pretreatment time and reaction temperature on CO{sub 2} capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor

Abstract

CO{sub 2} capture from flue gas using a sodium-based solid sorbent was investigated in a bubbling fluidized-bed reactor. Carbonation and regeneration temperature on CO{sub 2} removal was determined. The extent of the chemical reactivity after carbonation or regeneration was characterized via {sup 13}C NMR. In addition, the physical properties of the sorbent such as pore size, pore volume, and surface area after carbonation or regeneration were measured by gas adsorption method (BET). With water vapor pretreatment, near complete CO{sub 2} removal was initially achieved and maintained for about 1-2 min at 50{sup o}C with 2 s gas residence time, while without proper water vapor pretreatment CO{sub 2} removal abruptly decreased from the beginning. Carbonation was effective at the lower temperature over the 50-70{sup o}C temperature range, while regeneration more effective at the higher temperature over the 135-300{sup o}C temperature range. To maintain the initial 90% CO{sub 2} removal, it would be necessary to keep the regeneration temperature higher than about 135{sup o}C. The results obtained in this study can be used as basic data for designing and operating a large scale CO{sub 2} capture process with two fluidized-bed reactors.
Authors:
Seo, Y; Jo, S H; Ryu, C K; Yi, C K [1] 
  1. Korea Atomic Energy Research Institute, Taejon (Republic of Korea)
Publication Date:
Oct 15, 2007
Product Type:
Journal Article
Reference Number:
CLA-08:030068
Resource Relation:
Journal Name: Chemosphere; Journal Volume: 69; Journal Issue: 5
Subject:
01 COAL, LIGNITE, AND PEAT; CAPTURE; CARBON DIOXIDE; FLUIDIZED BED REACTORS; WATER VAPOR; FLUE GAS; ADSORBENTS; SODIUM COMPOUNDS; REGENERATION; TEMPERATURE DEPENDENCE
OSTI ID:
21004474
Country of Origin:
United Kingdom
Language:
English
Other Identifying Numbers:
Journal ID: ISSN 0045-6535; CMSHAF; TRN: 080300068
Submitting Site:
CLA
Size:
page(s) 712-718
Announcement Date:
Apr 14, 2008

Citation Formats

Seo, Y, Jo, S H, Ryu, C K, and Yi, C K. Effects of water vapor pretreatment time and reaction temperature on CO{sub 2} capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor. United Kingdom: N. p., 2007. Web. doi:10.1016/j.chemosphere.2007.05.036.
Seo, Y, Jo, S H, Ryu, C K, & Yi, C K. Effects of water vapor pretreatment time and reaction temperature on CO{sub 2} capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor. United Kingdom. https://doi.org/10.1016/j.chemosphere.2007.05.036
Seo, Y, Jo, S H, Ryu, C K, and Yi, C K. 2007. "Effects of water vapor pretreatment time and reaction temperature on CO{sub 2} capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor." United Kingdom. https://doi.org/10.1016/j.chemosphere.2007.05.036.
@misc{etde_21004474,
title = {Effects of water vapor pretreatment time and reaction temperature on CO{sub 2} capture characteristics of a sodium-based solid sorbent in a bubbling fluidized-bed reactor}
author = {Seo, Y, Jo, S H, Ryu, C K, and Yi, C K}
abstractNote = {CO{sub 2} capture from flue gas using a sodium-based solid sorbent was investigated in a bubbling fluidized-bed reactor. Carbonation and regeneration temperature on CO{sub 2} removal was determined. The extent of the chemical reactivity after carbonation or regeneration was characterized via {sup 13}C NMR. In addition, the physical properties of the sorbent such as pore size, pore volume, and surface area after carbonation or regeneration were measured by gas adsorption method (BET). With water vapor pretreatment, near complete CO{sub 2} removal was initially achieved and maintained for about 1-2 min at 50{sup o}C with 2 s gas residence time, while without proper water vapor pretreatment CO{sub 2} removal abruptly decreased from the beginning. Carbonation was effective at the lower temperature over the 50-70{sup o}C temperature range, while regeneration more effective at the higher temperature over the 135-300{sup o}C temperature range. To maintain the initial 90% CO{sub 2} removal, it would be necessary to keep the regeneration temperature higher than about 135{sup o}C. The results obtained in this study can be used as basic data for designing and operating a large scale CO{sub 2} capture process with two fluidized-bed reactors.}
doi = {10.1016/j.chemosphere.2007.05.036}
journal = []
issue = {5}
volume = {69}
place = {United Kingdom}
year = {2007}
month = {Oct}
}