Abstract
A theoretical investigation was conducted to study the transport-reaction process in the spray-drying flue gas desulfurization. A transport-reaction model of single particle was proposed, which considered the water evaporation from the surface of droplet and the reaction at the same time. Based on this model, the reaction rate and the absorbent utilization can be calculated. The most appropriate particle radius and the initial absorbent concentration can be deduced through comparing the wet lifetime with the residence time, the result shows in the case that the partial pressure of vapor in the bulk flue gas is 2000Pa, the optimum initial radius and absorbent concentration are 210∼310 μ m and 23% respectively. The model can supply the optimum parameters for semi-dry FGD system designed.
| Original language | English |
|---|---|
| Pages (from-to) | 356-360 |
| Journal | Journal of Thermal Science |
| Volume | 9 |
| Issue number | 4 |
| DOIs | |
| Publication status | Published - 2000 |
| Externally published | Yes |
Bibliographical note
Publication details (e.g. title, author(s), publication statuses and dates) are captured on an “AS IS” and “AS AVAILABLE” basis at the time of record harvesting from the data source. Suggestions for further amendments or supplementary information can be sent to [email protected].Research Keywords
- Chemical reaction
- Desulfurization
- Transfer-reaction process
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