Circulating fluidized bed semi-dry method desulfurization and dust removal twin-tower switching system and method and application
A semi-dry desulfurization and circulating fluidized bed technology, applied in the field of double-tower switching systems, can solve problems such as flue gas emission standards
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Embodiment 1
[0092] A circulating fluidized bed semi-dry desulfurization and dust removal double tower switching system, refer to figure 1 , including: the first desulfurization and dust removal tower, the second desulfurization and dust removal tower and switching system.
[0093]The first desulfurization and dust removal tower includes: a first desulfurization tower 1, a first dust remover 2, a first desulfurization silo 3, a first water tank 4 and a first induced draft fan 5; wherein, the first dust remover 2 and the second The upper part of a desulfurization tower 1 communicates; the first desulfurization bin 3 communicates with the bottom of the first desulfurization tower 1; the first water tank 4 is arranged above the first desulfurization bin 3 and communicates with the first desulfurization tower 1, The first induced draft fan 5 is arranged between the first dust collector 2 and the chimney 27 .
[0094] The second desulfurization and dust removal tower includes: a second desulfu...
Embodiment 2
[0100] A switching method of circulating fluidized bed semi-dry desulfurization and dedusting double towers during the load-up stage, refer to figure 2 , including the following steps:
[0101] (1) In the load-up stage, the flue gas volume gradually increases, and the single-tower operation state needs to be switched to the double-tower operation state. Assume that the first desulfurization and dust removal tower is in operation, and the second desulfurization and dust removal tower is not in operation. At this time, the main flue gas communication door 13 is opened, the first flue gas inlet door 14 is opened, and the rest of the doors are closed, the untreated first flue gas 28 and the second flue gas 29 enter the first flue gas duct 11 and the second flue gas duct 12 respectively Convergence in the first flue gas pipeline 11, then enter the first desulfurization and dust removal tower for desulfurization and dust removal;
[0102] (2) In the first stage, the net flue gas a...
Embodiment 3
[0131] A switching method of circulating fluidized bed semi-dry desulfurization and dedusting double towers during the load-up stage, refer to figure 2 , including the following steps:
[0132] (1) In the load-up stage, the flue gas volume gradually increases, and the single-tower operation state needs to be switched to the double-tower operation state. Assume that the first desulfurization and dust removal tower is in operation, and the second desulfurization and dust removal tower is not in operation. At this time, the main flue gas communication door 13 is opened, the first flue gas inlet door 14 is opened, and the rest of the doors are closed, the untreated first flue gas 28 and the second flue gas 29 enter the first flue gas duct 11 and the second flue gas duct 12 respectively Convergence in the first flue gas pipeline 11, then enter the first desulfurization and dust removal tower for desulfurization and dust removal;
[0133] (2) In the first stage, the net flue gas a...
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