Method and device for removing low-concentration sulfur dioxide in flue gas

A sulfur dioxide, low-concentration technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of large equipment, large volume, waste of sulfur resources, etc., to achieve enhanced contact effect, efficient mass transfer efficiency, The effect of prolonging the life cycle

Active Publication Date: 2011-04-20
JIANGSU ZEYU ENVIRONMENTAL ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Currently governing SO in the world 2 The main technical means of pollution is flue gas desulfurization. There are more than 200 kinds of flue gas desulfurization technologies researched, developed and used in various countries, of which about 20 kinds have been industrialized, and wet desulfurization is the main method. The principle is mostly based on alkali Absorbents absorb sulfur dioxide in flue gas, such as lime/limestone/gypsum method, ammonia method, etc. Most of the absorption equipment in these processes is tower equipment, which has problems such as large equipment volume, large floor area, high operating costs, and desulfurization The post-desulfurization products cannot be effectively treated. Even if some products have certain utilization value, most of them need to go through a series of processing before they can be used, and the development of their sales has become a big burden, so most of the desulfurization products are discarded. It only converts gas pollution into solid pollution, and causes waste of sulfur resources
[0003] Sodium citrate method flue gas desulfurization process belongs to renewable flue gas desulfurization process. Its absorption liquid has low vapor pressure and is non-toxic, which can effectively absorb sulfur dioxide in flue gas. The rich liquid after absorbing sulfur dioxide can be desorbed by steam heating and other methods to produce High-concentration sulfur dioxide is used as other chemical raw materials. After desorption, the barren liquid is continued to be used in the absorption process, which not only avoids secondary pollution, but also saves sulfur resources. However, most of the existing sodium citrate flue gas desulfurization processes use tower equipment for absorption. Not only is it bulky, it increases the investment and operation costs, but also the side reaction of sulfite radical oxidation is serious during the absorption process, and it is easy to generate a large

Method used

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  • Method and device for removing low-concentration sulfur dioxide in flue gas
  • Method and device for removing low-concentration sulfur dioxide in flue gas
  • Method and device for removing low-concentration sulfur dioxide in flue gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Adjust the rotating speed of the rotary packed bed 5 to be 500r / min, the absorption solution with a citric acid concentration of 0.1mol / L and a pH value of 6 is added to the rotary packed bed 5 through the liquid inlet 5.1 of the rotary packed bed, and the mass concentration of sulfur dioxide is 2000mg / m 3 The simulated flue gas enters the rotating packed bed 5 through the rotating packed bed gas inlet 5.3, the absorption temperature is 40°C, and the gas flow rate is 60m 3 / h, adjust the liquid-gas ratio to 7 (L / m 3 ), the gas phase and the liquid phase contact and react rapidly in the rotating packed bed 5, the purified gas is discharged from the rotating packed bed gas outlet 5.2, and the citrate solution dissolved in sulfur dioxide is discharged from the rotating packed bed liquid outlet 5.5, and is desorbed by the desorption system After returning to the absorption system for recycling, the gas-liquid ratio of the desorption operation is 900m 3 / m 3 , the desorpti...

Embodiment 2

[0039] Adjust the rotational speed of the rotary packed bed 5 to be 1000r / min, add the absorption solution with a concentration of citric acid of 1.5mol / L and a pH value of 2 to the rotary packed bed 5 through the liquid inlet 5.1 of the rotary packed bed, and the mass concentration of sulfur dioxide is 8500g / m 3 The simulated flue gas enters the rotary packed bed 5 through the rotary packed bed gas inlet 5.3, the absorption temperature is 30°C, and the gas flow rate is adjusted to 30m 3 / h, adjust the liquid-gas ratio to 4 (L / m 3 ), the gas phase and the liquid phase contact and react rapidly in the rotating packed bed 5 . The purified gas is discharged from the gas outlet 5.2 of the rotating packed bed, and the citrate solution dissolved in sulfur dioxide is discharged from the liquid outlet 5.5 of the rotating packed bed. After being desorbed by the desorption system, it is returned to the absorption system for recycling. The gas-liquid ratio of the desorption operation is ...

Embodiment 3

[0041] Adjust the rotational speed of the rotary packed bed 5 to be 3000r / min, add the absorption solution with a citric acid concentration of 1.0mol / L and a pH value of 4.5 to the rotary packed bed 5 through the liquid inlet 5.1 of the rotary packed bed, and the mass concentration of sulfur dioxide is 5000g / m 3 The simulated flue gas enters the rotary packed bed 5 through the rotary packed bed gas inlet 5.3, the absorption temperature is 60°C, and the gas flow rate is adjusted to 40m 3 / h to adjust the liquid-gas ratio to 3 (L / m 3 ), the gas phase and the liquid phase contact and react rapidly in the rotating packed bed 5 . The purified gas is discharged from the gas outlet 5.2 of the rotating packed bed, and the citrate solution dissolved in sulfur dioxide is discharged from the liquid outlet 5.5 of the rotating packed bed. After being desorbed by the desorption system, it is returned to the absorption system for recycling. The gas-liquid ratio of the desorption operation is...

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Abstract

The invention belongs to the technical field of flue gas desulfurization, in particular to a method and device for removing low-concentration sulfur dioxide in flue gas, thereby solving the shortcomings in the existing flue gas desulfurization process. A citric acid-sodium citrate buffer solution is taken as an absorption solution, a rotary packed bed is taken as an absorption reactor, and the method comprises the steps of opening the rotary packed bed, leading the absorption solution and the flue gas containing the sulfur dioxide to enter into the rotary packed bed, leading a liquid phase and a gas phase to conduct the contact reaction, and leading the liquid phase after the reaction to enter into a desorption system for desorption. The device comprises the rotary packed bed, a gas inletof the rotary packed bed is connected with a source of the flue gas containing the sulfur dioxide, a liquid inlet of the rotary packed bed is connected with the source of the absorption solution, anda liquid outlet of the rotary packed bed is connected with the desorption system. By adopting the method, the desulfurization efficiency is high, the absorption solution is renewable, and the method can be flexibly used in an acid-making system or systems for producing sulfur and the like; furthermore, the device can reduce scale formation and blockage of the device, be conductive to improving the absorption efficiency and the desorption rate of the absorption solution and reduce the investment and the operation cost.

Description

technical field [0001] The invention belongs to the technical field of flue gas desulfurization, and specifically relates to a method and a device for removing low-concentration sulfur dioxide in flue gas by using a citric acid-sodium citrate buffer solution as an absorbent and a high-gravity rotating packed bed as an absorption reactor. Background technique [0002] Sulfur dioxide in flue gas is extremely harmful to animals, plants and the ecological environment, especially for low-concentration sulfur dioxide. Due to its high content in flue gas and low treatment benefits, its effective treatment has become a major problem for a long time. Currently governing SO in the world 2 The main technical means of pollution is flue gas desulfurization. There are more than 200 kinds of flue gas desulfurization technologies researched, developed and used in various countries, of which about 20 kinds have been industrialized, and wet desulfurization is the main method. The principle is...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D53/50B01D53/96
Inventor 刘有智姜秀平
Owner JIANGSU ZEYU ENVIRONMENTAL ENG
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