AbstractA cascade‐scrubbing technology was proposed to improve the current once‐through desulfurization solutions. Desulfurization experiments were performed for a 162‐kW marine diesel engine's exhaust gas so as to confirm the alkali‐lean/alkali‐rich lye cascade‐scrubbing advantages compared with the closed‐loop solution. In the closed‐loop scrubbing model, desulfurization efficiency presented multiple change patterns, such as initially decreasing but then increasing with the liquid–gas ratio, decreasing with SO2 concentration, and increasing with Na/S. At the high SO2 concentration of 2,860 mg/Nm3 and Na/S = 2, desulfurization complying with emission control area's (ECA's) requirements necessitated a liquid–gas ratio above 4.5 L/Nm3. Although raising Na/S could decrease the liquid–gas ratio requirement, the alkali‐utilization efficiency dropped. In the alkali‐lean/alkali‐rich lye cascade‐scrubbing model under the same SO2 and Na/S conditions, the auxiliary scrubbing section allowed a desulfurization capacity of 500–750 mg/Nm3 with an alkali‐rich liquid–gas ratio of 1–2 L/Nm3. With the alkali‐rich lye fed at liquid–gas ratios of 1, 1.5, and 2 L/Nm3, the main scrubbing section's alkali‐lean lye necessitated liquid–gas ratios of 2.8, 2.4, and 3.1 L/Nm3 to comply with ECA's requirements, respectively. Two setups approaching the former two liquid–gas ratio assembles (i.e., a total liquid–gas ratio of 4 L/Nm3 gaining a high alkali‐utilization efficiency above 98%) thus confirmed that this cascade‐scrubbing model was superior to the closed‐loop solution in cutting the liquid–gas ratio requirement and alkali consumption, because of the latter necessitating a liquid–gas ratio of 4.5 L/Nm3 at Na/S = 2 or 4 L/Nm3 at Na/S = 2.16 but with the alkali‐utilization efficiency dropping below 91%.
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