dc.contributor.author |
Ebune, Guilbert Ebune. |
|
dc.contributor.other |
Youngstown State University. Department of Environmental Studies. |
|
dc.date.accessioned |
2021-10-19T15:33:47Z |
|
dc.date.available |
2021-10-19T15:33:47Z |
|
dc.date.issued |
2008 |
|
dc.identifier.other |
B2038239x |
|
dc.identifier.other |
276949830 |
|
dc.identifier.uri |
https://jupiter.ysu.edu:443/record=b2038239 |
|
dc.identifier.uri |
http://hdl.handle.net/1989/16666 |
|
dc.description |
viii, 42 leaves : ill. ; 29 cm. Thesis (M.S.)--Youngstown State University, 2008. Includes bibliographical references (leaves 39-42). |
en_US |
dc.description.abstract |
Adsorption is considered one of the more promising technologies for capturing CO2 from flue gases. This research shows an efficient chemical adsorption method capable of capturing carbon dioxide under moist conditions from flue gases of coal-fired power plants. Carbon dioxide was chemically adsorbed by the reaction K2CO3*1.5H2O + CO2 ↔ 2KHCO3 + 0.5H2O + heat. Moisture however, plays a significant role in the chemical adsorption process, which readily facilitates the adsorption process. Moisture usually contained as high as 8-17% in flue gases, badly affects the capacity of conventional adsorbents such as zeolites, but the present technology has no concern with moisture; water is rather necessary in principle as shown in the equation above. Carbon dioxide uptake occurred at a temperature of 60°C and the entrapped carbon dioxide was released by the decomposition of potassium bicarbonate to shift the reaction in the reverse direction. The decomposition occurred at high enough temperatures of 150°C to ensure complete regeneration of the sorbent. For the purpose of this research, emphasis was placed more on the adsorption process. When compared to other processes such as the conventional amine process, it provided an efficient, low utility cost and energy-conservative effect. The activated carbon was prepared by 20% by weight of K2CO3 and samples used during the experimental runs were dried at 60°C for the 26-hour runs and at 25°C and 125°C for the air-dried and oven-dried samples respectively for the 48-hour runs. The samples all got to the saturation point after 6 hours of exposure to carbon dioxide and gave adsorption capacities in the range of 2.5 to 3.5mol CO2/mol K2CO3 for all experimental runs performed in this research. |
en_US |
dc.description.sponsorship |
Youngstown State University. Department of Environmental Studies. |
en_US |
dc.language.iso |
en_US |
en_US |
dc.relation.ispartofseries |
Master's Theses;no. 1116 |
|
dc.subject |
Carbon dioxide -- Absorption and adsorption. |
en_US |
dc.subject |
Flue gases -- Purification. |
en_US |
dc.subject |
Coal-fired power plants -- Environmental aspects. |
en_US |
dc.subject |
Greenhouse gases -- Environmental aspects. |
en_US |
dc.title |
Carbon dioxide capture from power plant flue gas using regenerable activated carbon powder impregnated with potassium carbonate |
en_US |
dc.type |
Thesis |
en_US |