Modified calcium-based desulfurizing agent for dry desulfurization of sintering gas and preparation method of modified calcium-based desulfurizing agent
A technology for dry desulfurization and sintering flue gas, which is applied in separation methods, chemical instruments and methods, and dispersed particle separation, etc., can solve the problems of complex preparation process and high price, and achieve simple preparation process, low price, and optimized organizational structure. Effect
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Embodiment 1
[0022] First mix 85wt% of limestone, 10wt% of municipal domestic sludge, and 5wt% of anthracite coal powder, and set aside; then put the mixed raw materials into a rotary kiln, calcinate at 1100°C for 30min, and cool naturally with the furnace. After being released from the furnace, the material is ground to a particle size of 0.1-0.2mm, and a modified calcium-based desulfurizer for dry desulfurization of sintering flue gas is obtained.
[0023] The modified calcium-based desulfurizer is used in the sintering flue gas for simulated desulfurization treatment, and the O in the sintering flue gas 2 The content is 14vol%, CO 2 The content is 7vol%, H 2 The O content is 10vol%, the SO2 content is 1000ppm, the reaction temperature is 90°C, Ca / S=1.4, the cycle rate is 100, and the H 2 The desulfurization treatment was carried out under the condition of O / CaO=1.6, and the residence time was 0.8s, and the desulfurization efficiency reached 93.8%.
Embodiment 2
[0025] First mix 88wt% of limestone, 8wt% of municipal domestic sludge, and 4wt% of anthracite coal powder, and set aside; then put the mixed raw materials into a rotary kiln, calcinate at 1000 ° C for 20 minutes, and cool naturally with the furnace. After being released from the furnace, the material is ground to a particle size of 0.1-0.2mm, and a modified calcium-based desulfurizer for dry desulfurization of sintering flue gas is obtained.
[0026] The modified calcium-based desulfurizer is used in the sintering flue gas for simulated desulfurization treatment, and the O in the sintering flue gas 2 The content is 18vol%, CO 2 The content is 5vol%, H 2 O content is 8vol%, SO 2 The content is 800ppm, the reaction temperature is 140°C, Ca / S=1.5, the cycle rate is 130, and the H 2 O / CaO=1.7, and the desulfurization treatment is carried out under the condition of the residence time of 1.1s, and the desulfurization efficiency reaches 95.6%.
Embodiment 3
[0028] First mix 92wt% of limestone, 5wt% of municipal domestic sludge, and 3wt% of anthracite coal powder, and set aside; then put the mixed raw materials into a rotary kiln, calcinate at 1050°C for 25min, and cool naturally with the furnace. After being released from the furnace, the material is ground to a particle size of 0.1-0.2mm, and a modified calcium-based desulfurizer for dry desulfurization of sintering flue gas is obtained.
[0029] The modified calcium-based desulfurizer is used in the sintering flue gas for simulated desulfurization treatment, and the O in the sintering flue gas 2 The content is 16vol%, CO 2 The content is 4vol%, H 2 O content is 9vol%, SO 2 The content is 900ppm, the reaction temperature is 120°C, Ca / S=1.6, the cycle rate is 150, and the H 2 O / CaO=1.8, and the residence time is 1.2s for desulfurization, and the desulfurization efficiency reaches 99.6%.
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