Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
9451686 | Chemosphere | 2005 | 7 Pages |
Abstract
An innovative catalyst system has been developed to simultaneously remove NO and SO2 from combustion flue gas. Such catalyst system may be introduced to the scrubbing solution using ammonia solution to accomplish sequential absorption and catalytic oxidation of both NO and SO2 in the same reactor. When the catalyst system is utilized for removing NO and SO2 from the flue gas, Co(NH3)62+ ions act as the catalyst and Iâ as the co-catalyst. Dissolved oxygen, in equilibrium with the residual oxygen in the flue gas, is the oxidant. The overall removal process is further enhanced by UV irradiation at 365Â nm. More than 95% of NO is removed at a feed concentration of 250-900Â ppm, and nearly 100% of SO2 is removed at a feed concentration of 800-2500Â ppm. The sulfur dioxide co-existing in the flue gas is beneficial to NO absorption into hexamminecobalt(II)/iodide solution. NO and SO2 can be converted to ammonium sulfate and ammonium nitrate that can be used as fertilizer materials. The process described here demonstrates the feasibility of removing SO2 and NO simultaneously only by retrofitting the existing wet ammonia flue-gas-desulfurization (FGD) scrubbers.
Related Topics
Life Sciences
Environmental Science
Environmental Chemistry
Authors
Xiang-li Long, Wen-De Xiao, Wei-kang Yuan,