Alkali liquor method for flue gas desulfurization
A technology of lye and flue gas, which is applied in the field of environmental engineering, can solve the problems of high price and increased operating cost, and achieve the effect of reducing consumption, reducing treatment cost and ensuring desulfurization rate
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Embodiment 1
[0014] The residual ammonia water of a coking plant was used to replace 20% of the start-up base. The ammonia nitrogen content in the residual ammonia water used in the test was 3200 mg / L, and the amount of additive A added was 0.3 mg / L; the SO in the test flue gas 2 The average concentration is 2000mg / m 3 ; The average flow rate of flue gas is 600L / min; the average temperature of flue gas at the system inlet is 60°C; the remaining ammonia water and starting alkali are added to the desulfurization tower respectively. Among them, NaOH is used as the starting base, the concentration is 0.4mol / L, and the liquid-gas ratio is 2L / m 3 ; SO in the treated flue gas 2 The concentration is 100mg / m 3 , the desulfurization rate reaches 95.0%. The system can run continuously and stably, and the material circulation in the system is smooth.
Embodiment 2
[0016] Replace 50% of the start-up alkali with the residual ammonia water of a coking plant. The ammonia nitrogen content in the residual ammonia water used in the test is 3200 mg / L, and the addition amount of additive A is 0.3 mg / L; the SO in the test flue gas 2 The average concentration is 2000mg / m 3 ; The average flue gas flow rate is 600L / min; the average temperature of the flue gas at the system inlet is 60°C; the remaining ammonia water and starting alkali are respectively added to the desulfurization tower, and the starting alkali is NaOH, the concentration is 0.4mol / L, and the liquid-gas ratio is 2L / m 3 ; SO in the treated flue gas 2 The concentration is 72mg / m 3 , the desulfurization rate reached 96.4%. The system can run continuously and stably, and the material circulation in the system is smooth.
Embodiment 3
[0018] Replace 80% of the start-up alkali with the residual ammonia water of a coking plant. The ammonia nitrogen content in the residual ammonia water used in the test is 3200mg / L, and the addition amount of additive A is 0.3mg / L; the SO in the test flue gas 2 The average concentration is 2000mg / m 3 ; The average flue gas flow rate is 600L / min; the average temperature of the flue gas at the system inlet is 60°C; the remaining ammonia water and starting alkali are respectively added to the desulfurization tower, and the starting alkali is NaOH, the concentration is 0.4mol / L, and the liquid-gas ratio is 2L / m 3 ; SO in the treated flue gas 2 The concentration is 106mg / m 3 , the desulfurization rate reached 94.70%. The system can run continuously and stably, and the material circulation in the system is smooth.
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