Process for cleaning flue gases by utilizing alkali resources in slag
A technology for flue gas and slag, which is applied in the separation of dispersed particles, chemical instruments and methods, separation methods, etc., can solve the problems of increasing the cost of heat treatment of waste, save water resources and treatment costs, improve economic benefits, and reduce treatment costs. cost effect
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Embodiment 1
[0026] A domestic waste incineration device has a capacity of 200t / d, and the average mass of solid residue discharged per ton of domestic waste is 155Kg / d, and the flue gas produced after ton of waste incineration is about 2980Nm 3 , in volume fraction, the flue gas contains CO 2 5%, SO 2 266mg / m 3 ; NOx (in NO 2 In terms of) 800mg / m 3 ;HCl is 196mg / m 3 ;HF is 56mg / m 3 , the flue gas temperature is 920°C.
[0027]With the process of the present invention, the high-temperature flue gas enters the heat utilization system E1 through the high-temperature flue gas conveying pipe 3 to generate high-pressure water vapor, which is used for power generation and heating and cooling of the factory area. After heat utilization, the temperature of the flue gas drops to 118°C, and passes through the low-temperature flue gas pipeline 4 into the bottom of No. 1 reaction absorption tower T1. The temperature of the slag at the bottom of the domestic waste incinerator F1 is 905°C. It is ...
Embodiment 2
[0030] A pyrolysis-gasification combustion facility with a processing capacity of 300t / d domestic waste in a certain place, the average solid slag discharged from the pyrolysis gasifier per ton of domestic waste is 148Kg, and the gas combustion system produces 2890Nm of flue gas 3 , the flue gas contains CO 2 6.2%, SO 2 221mg / m 3 ; NOx (in NO 2 In terms of) 780mg / m 3 ; HCl is 202mg / m 3 ;HF is 35mg / m 3 , the flue gas temperature is 1048°C. The pH of the cooled and prepared alkaline solution in S2 is 8.2. The operating pressure of No. 1 reaction absorption tower T1 is 0.14MPa, the operating temperature is 16°C, and the liquid phase spray density is 28m 3 / (m 2 h). The operating pressure of No. 2 reaction absorption tower T2 is 0.135MPa, the operating temperature is 25°C, and the liquid phase spray density is 30m 3 / (m 2 h). The method of operation is the same as in Example 1.
[0031] After passing the above steps, the content of various acidic substances in the flue...
Embodiment 3
[0033] A pyrolysis-gasification combustion facility with a processing capacity of 120t / d domestic waste in a certain place, the average solid slag discharged from the pyrolysis gasifier per ton of domestic waste is 163Kg, and the gas combustion system produces 3108Nm of flue gas 3 , the flue gas contains CO 2 5.3%, SO 2 198mg / m 3 ; NOx (in NO 2 In terms of) 669mg / m 3 ; HCl is 254mg / m 3 ; HF is 67mg / m 3 , the flue gas temperature is 1032°C. The pH of the cooled and prepared alkali solution in S2 is 9.0. The operating pressure of No. 1 reaction absorption tower T1 is 0.125MPa, the operating temperature is 11°C, and the liquid phase spray density is 22m 3 / (m 2 h). The operating pressure of No. 2 reaction absorption tower T2 is 0.12MPa, the operating temperature is 28°C, and the liquid phase spray density is 27m 3 / (m 2 h). Operation method is the same with embodiment 1,2.
[0034] After passing the above steps, the content of various acidic substances in the flue gas...
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