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Application method of fine desulfurization in sulfuric acid exhaust absorption

An application method, fine desulfurization technology, applied in separation methods, chemical instruments and methods, separation of dispersed particles, etc.

Active Publication Date: 2013-04-17
云南云天化云峰化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Defects of the existing technology: the conversion catalyst needs to rely on imported foreign catalysts; the cost is high; the exhaust SO2 emission reaches 500--600mg / Nm3, exceeding the emission standard allowed by the country
[0004]At present, my country's environmental pollution is serious, and the trend of ecological damage has not been effectively controlled, and sulfur dioxide emissions will form acid rain

Method used

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  • Application method of fine desulfurization in sulfuric acid exhaust absorption
  • Application method of fine desulfurization in sulfuric acid exhaust absorption

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] A. Introduce the sulfur-containing tail gas into the recovery tower;

[0032] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 5.6 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 370:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 87%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank, in order to ensure that the ammonium sulfite-ammonium bisulfite solution (NH 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.3% dilute ammonia to a...

Embodiment 2

[0036] A. Introduce the sulfur-containing tail gas into the recovery tower;

[0037] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 6.1 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 350:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 82%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank, in order to ensure that the ammonium sulfite-ammonium bisulfite solution (NH 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.46% dilute ammonia to ...

Embodiment 3

[0041] A. Introduce the sulfur-containing tail gas into the recovery tower;

[0042] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 5.8 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 360:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 93%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank. 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.5% dilute ammonia to adjust.

[0043] C. Add sulfuric acid to decompose in step B: the excess moth...

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Abstract

The invention discloses an application method of fine desulfurization in sulfuric acid exhaust absorption, and relates to a technical scheme of the application of fine desulfurization in sulfuric acid exhaust absorption, in particular to a method for discharging SO2 exhaust. The method comprises the following steps of: A, introducing sulfur-containing exhaust into an absorption tower; and B, spraying ammonium sulfite-ammonium hydrogen sulfite solution serving as a fine desulfurization solution with the pH value of 5.6 to 6.1 from the top of the tower to absorb SO2 and SO3 in the sulfur-containing exhaust, and regulating the gas-liquid ratio to be (350-370): 1, wherein according to the concentration of aqueous ammonia in step B, the absorption mother solution refluxes to a mother solution circulating tank from the bottom of the absorption tower, and 10.3 to 10.6 mass percent of diluted aqueous ammonia is added, so that the ratio of (NH4)2SO3 to NH4HSO3 in the absorption solution is unchanged in an optimal range of the ammonium sulfite-ammonium hydrogen sulfite solution serving as the fine desulfurization solution; and the temperature of the mother solution in step B is between 25 and 30 DEG C. After the sulfur-containing exhaust is treated, the conversion rate of a sulfur acid device is more than or equal to 99.5 percent, and 60mg / Nm<3> of SO2 exhaust is discharged; and by substituting the expensive imported accelerant for the cheap domestic accelerant, the national emission standard can also be achieved, and the cost is reduced.

Description

technical field [0001] The invention relates to a technical scheme for the application of fine desulfurization in sulfuric acid tail suction, in particular to tail gas SO 2 method of emission. [0002] Background technique [0003] Defects of the existing technology: the conversion catalyst needs to rely on imported foreign catalysts; the cost is high; the tail gas SO 2 Emission reaches 500--600mg / Nm 3 , Exceeding the emission standard allowed by the state. [0004] At present, my country's environmental pollution is serious, and the trend of ecological damage has not been effectively controlled, and sulfur dioxide emissions will form acid rain. Energy conservation and emission reduction has become the most economical and effective measure to reduce environmental pollution and slow down global warming. With the strengthening of the country's control over emissions, starting from the company's own interests and social responsibilities, it is necessary to control sulfur d...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/50
Inventor 念吉红
Owner 云南云天化云峰化工有限公司
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