Novel desulfurization method for calcination tail gas
A tail gas and calcination technology, applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve problems such as unsatisfactory treatment effects of tail gas desulfurization devices, failure to meet national emission standards, and difficulty in recycling and reuse, etc., to achieve increased Recycling and processing value, reducing enterprise investment and operating production costs, and reducing the effect of water mist
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Embodiment 1
[0035] The calcined tail gas desulfurization method of the operating section comprises the following steps:
[0036] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the waste sulfuric acid circulation spray period is 7 days, part of the waste sulfuric acid after concentration is transported to the thickened acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;
[0037] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spr...
Embodiment 2
[0045] Calcination tail gas desulfurization method, comprising the steps of:
[0046] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the waste sulfuric acid circulation spray period is 3 days, part of the waste sulfuric acid after thickening is transported to the concentrated acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;
[0047] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spray liquid obtained after sand f...
Embodiment 3
[0051] Calcination tail gas desulfurization method, comprising the steps of:
[0052] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the cycle spraying period of waste sulfuric acid is 9 days, part of the waste sulfuric acid after thickening is transported to the concentrated acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;
[0053] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spray liquid obtained after sand f...
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