Desulfurizing tower and chimney integration device
A desulfurization tower and chimney technology, which is applied in the field of desulfurization tower and chimney integrated device, can solve the problems of large flue gas flow resistance, long flue, clean flue and its support cost, and reduce flue gas resistance and manufacturing cost Reduce and save the effect of smoke exhaust power consumption
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Embodiment 1
[0036] 300,000-kilowatt coal-fired heating unit project, two 350MW supercritical coal-fired units, wet desulfurization, one furnace and one tower, the diameter of the desulfurization tower is 13m, and the height of the tower is 33m. The two units share a 210m chimney, the bottom inner diameter of the outer cylinder of the chimney is 20m, and the inner diameter of the top is 10.6m. The chimney uses a single bundled inner cylinder with a diameter of 7.8m;
[0037] To adopt the combined device of the desulfurization tower and the chimney of this patent, the diameter of the lower part of the outer cylinder of the chimney needs to be expanded to about 45m, and the height of the lower part is more than 35m. It can be restored to the normal cylinder diameter (15m) at an elevation of about 55m. Between 35m and 55m, a structural transition layer is used for transition, and the flue gas at the outlet of the desulfurization tower is pushed out and merged, and then connected to the inner ...
Embodiment 2
[0039] 600,000-kilowatt coal-fired unit project, two 660MW ultra-supercritical coal-fired units, wet desulfurization, one furnace and one tower, the diameter of the desulfurization tower is 16.8m, and the height of the tower is 44m. The two units share a 240m chimney. The inner diameter of the chimney outer cylinder is 30.4m at the bottom and 13.4m at the top. The chimney uses a single cluster inner cylinder with a diameter of 10.5m;
[0040] To adopt the combined device of the desulfurization tower and the chimney of this patent, the diameter of the lower part of the outer cylinder needs to be expanded to about 51m, and the height of the lower part is more than 45m. It can be restored to the normal cylinder diameter (22.6m) at an elevation of about 65m. Between 45m and 65m, a structural transition layer is used for transition, and the flue gas at the outlet of the desulfurization tower is pushed out and merged, and then connected to the inner tube of the chimney.
Embodiment 3
[0042] 1 million kilowatt-class coal-fired unit project, two 1000MW ultra-supercritical coal-fired units, wet desulfurization, one furnace and one tower, the diameter of the desulfurization tower is 22.2m, and the height of the tower is 44m. The two units share a 240m chimney, the bottom inner diameter of the outer cylinder of the chimney is 35.5m, and the inner diameter of the top is 21.2m. The chimney adopts a double cluster inner cylinder with a diameter of 9.0m;
[0043] To adopt the combination device of the desulfurization tower and the chimney of this patent, the diameter of the lower part of the outer cylinder needs to be expanded to 64m, and the height of the lower part is more than 45m. It can be restored to the normal cylinder diameter (27.4m) at an elevation of about 70m. Between 45m and 70m, a structural transition layer is used for transition, and the flue gas at the outlet of the desulfurization tower is ejected and connected to the inner tube of the chimney.
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