Sodium-based dry regenerable sorbent for carbon dioxide capture from power plant flue gas
- Authors
- Lee, Joong B.; Ryu, Chong K.; Baek, Jeom-In; Lee, Ji H.; Eom, Tae H.; Kim, Sung Hyun
- Issue Date
- 2-Jul-2008
- Publisher
- AMER CHEMICAL SOC
- Keywords
- Regenerable sorbent; carbon dioxide; capture; power plant; flue gas
- Citation
- INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, v.47, no.13, pp 4465 - 4472
- Pages
- 8
- Indexed
- SCIE
SCOPUS
- Journal Title
- INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
- Volume
- 47
- Number
- 13
- Start Page
- 4465
- End Page
- 4472
- URI
- https://scholar.korea.ac.kr/handle/2021.sw.korea/123042
- DOI
- 10.1021/ie0709638
- ISSN
- 0888-5885
1520-5045
- Abstract
- Dry regenerable sorbent technology is one of the emerging technologies as a cost-effective and energy-efficient technology for CO2 capture from flue gas. Six sodium-based dry regenerable sorbents were prepared by spray-drying techniques. Their physical properties and reactivities were tested to evaluate their applicability to a fluidized-bed or fast transport-bed CO2 capture process. Each sorbents contained 20-50 wt% of Na2CO3 or NaHCO3. All sorbents except for Sorb NX30 were insufficient with either attrition resistance or reactivity, or both properties. Sorb NX30 sorbent satisfied most of the physical requirements for a commercial fluidized-bed reactor process along with good chemical reactivity. Sorb NX30 sorbent had a spherical shape, an average size of 89 mu m, a size distribution of 38-250 mu m, and a bulk density of approximately 0.87 g/mL. The attrition index (AI) of Sorb NX30 reached below 5% compared to about 20% for commercial fluidized catalytic cracking (FCC) catalysts. CO2 sorption capacity of Sorb NX30 was approximately 10 wt% (>80% sorbent utilization) in the simulated flue gas condition compared with 6 of 30 wt% MEA solution (33% sorbent utilization). All sorbents showed almost-complete regeneration at temperatures less than 120 degrees C.
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