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

Inactive Publication Date: 2014-01-29
武汉钢铁有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process operation of desulfurizing sintering flue gas with calcium-based desulfurizer, the cost of desulfurizer accounts for a large proportion of the operation cost of flue gas desulfurization. In order to improve the desulfurization efficiency of calcium-based desulfurizer, the current common method is to use chemical solution Condition the calcium-based desulfurizer to optimize the digestion process and improve the characteristics of the digested product, thereby improving the microstructure of the calcium-based desulfurizer, reducing the diffusion resistance of the gas phase in the pores of the desulfurizer during the desulfurization process, and improving the desulfurization efficiency of the calcium-based desulfurizer However, the use of chemical solutions to temper desulfurizers has defects such as complex preparation process and high price. Therefore, the development of high-efficiency, low-cost, and wide-source desulfurizers is a common problem faced by the desulfurization industry.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses a modified calcium-based desulfurizing agent for dry desulfurization of sintering gas and a preparation method of the modified calcium-based desulfurizing agent. The desulfurizing agent comprises the following raw material components in weight percent: 85-95% of limestone, 2.5-10% of urban domestic sludge and 2.5-6% of anthracite duff. A preparation method comprises the following steps: 1) uniformly mixing the limestone, the urban domestic sludge and the anthracite duff according to the proportions for further use; and 2) roasting the mixed raw materials for 20-30 minutes at 1000-1100 DEG C, naturally cooling to normal temperature, and crushing the materials until the grain size is 0.1-0.2mm, thus obtaining the modified calcium-based desulfurizing agent for dry desulfurization of sintering gas. The modified calcium-based desulfurizing agent for dry desulfurization of sintering gas, prepared by using the preparation method disclosed by the invention, has the advantages that the desulfurization efficiency for the sintering gas is over 93 percent, the preparation process is simple, and the raw materials are wide in source and low in cost.

Description

technical field [0001] The invention relates to flue gas desulfurization technology, in particular to a modified calcium-based desulfurizer for dry desulfurization of sintering flue gas and a preparation method thereof. Background technique [0002] Calcium-based desulfurizers are widely used because of their low price and wide range of sources. As flue gas desulfurizers, commonly used calcium-based desulfurizers include lime, slaked lime, carbide slag, limestone, and dolomite. The activity of calcium-based desulfurizers is mainly determined by the particle size, specific surface area, pore size distribution of calcium-based desulfurizers, and the diffusion rate of reactants through the sulfide product layer. Therefore, even under the same Ca / S, different calcium The desulfurization efficiency of the base desulfurizer is different. The reactivity of the desulfurizer is one of the key factors affecting the effect of flue gas desulfurization. The higher the activity of the de...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/50B01D53/81
Inventor 莫亚平陈旺生孙庆星秦林波汤静芳韩军蒋国波杨慧张九红李富智
Owner 武汉钢铁有限公司
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