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Simultaneous desulphurization and denitration device for seawater smoke with membrane absorption method, as well as process of device

A technology of desulfurization, denitrification, and membrane absorption, which is applied in separation methods, air quality improvement, chemical instruments and methods, etc., can solve the problems of limited adjustment range, difficulty in resisting impact, equipment corrosion, etc., to achieve wide application range, prevent water vapor, The effect of mitigating corrosion

Active Publication Date: 2013-10-02
TIANJIN SEA WATER DESALINATION & COMPLEX UTILIZATION INST STATE OCEANOGRAPHI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since the devices used are gas absorption equipment (such as packed towers, liquid column towers and spray towers, etc.), they still cannot get rid of the common problems of wet flue gas desulfurization: the gas-liquid two-phase is completely mixed and contacted, and the adjustment range is limited. Difficult to resist high concentrations of SO 2 and NO X The impact of the flue gas absorption process; the gas-liquid two-phase direct contact, the discharged flue gas contains a large amount of water vapor, and the equipment corrosion problem is serious

Method used

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  • Simultaneous desulphurization and denitration device for seawater smoke with membrane absorption method, as well as process of device
  • Simultaneous desulphurization and denitration device for seawater smoke with membrane absorption method, as well as process of device

Examples

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Embodiment 1

[0067] The simultaneous desulfurization and denitrification process of seawater flue gas by membrane absorption method is adopted as shown in the attached figure. The desulfurization and denitrification core part of the device is composed of three-stage box-type hydrophobic hollow fiber membrane absorbers 1-1, 1-2 and 1-3 in horizontal series. Assembled, the hollow fiber membrane filling area of ​​each stage membrane absorber is 500m 2 , the film packing density is about 9%; the pretreated raw seawater 2 is used as the seawater-based absorbent, the pH value is 8.2, and the temperature is normal temperature; the actual coal-fired flue gas is used, and its SO 2 The concentration is 1500mg / Nm 3 , NO X Concentration 350mg / m 3 , soot concentration 100mg / Nm 3 , the temperature is 110℃~120℃, the flue gas treatment capacity is 1000Nm 3 / h. The continuous monitoring device for flue gas components is selected as SWG300 -1 Smoke is in the monitoring system. Using hydrogen peroxide...

Embodiment 2

[0069] Using the same membrane absorption treatment device and flue gas oxidant as in Example 1, the flue gas condition is SO 2 The concentration is 1500mg / Nm 3 , NO X Concentration 650mg / m 3 , soot concentration 100mg / Nm 3 , the temperature is 110℃~120℃, the flue gas treatment capacity is 1000Nm 3 / h. And using seawater-based NaClO 2 solution as an absorbent, where the additive NaClO 2 The concentration is 0.0004mol / L, the pH value is 9.0, and the temperature is normal temperature; after stable operation, the molar ratio of the amount of hydrogen peroxide sprayed into the oxidant injection device 9 to the amount of nitric oxide in the flue gas is 1.1, and the flow rate of seawater-based absorbent is 10m 3 / h, flue gas 17SO after desulfurization and denitrification 2 The concentration is 100mg / Nm 3 , NO X The concentration is 100mg / m 3 , the post-treatment of desulfurized and denitrified seawater is the same as in Example 1. Example 3:

Embodiment 3

[0070] Using the same flue gas conditions, flue gas oxidant and membrane absorption treatment device as in Example 1, the seawater-based absorbent used is composed of former seawater and NaClO 2 and HCl two additives, of which NaClO 2 The concentration is 0.0004mol / L, the concentration of HCl is 0.0001mol / L, the pH value is 6.0, and the temperature is normal temperature; after stable operation, the molar ratio of the amount of hydrogen peroxide injected into the oxidant injection device 9 to the amount of nitric oxide in the flue gas is 1.1 , the flow rate of seawater-based absorbent is 8m 3 / h, flue gas 17SO after desulfurization and denitrification 2 The concentration is 100mg / Nm 3 , NO X The concentration is 100mg / m 3 After desulfurization and denitrification, the absorption liquid and cleaning seawater are collectively discharged into the treatment tank, mixed with fresh seawater and mixed with waste alkali for neutralization, and aerated to restore the water quality, ...

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Abstract

The invention discloses a simultaneous desulphurization and denitration device for seawater smoke with a membrane absorption method. The device comprises at least one level of hydrophobic hollow fiber membrane absorber. A process of the device comprises steps as follows: firstly, nitric oxide in the smoke performs an oxidizing reaction to generate nitrogen dioxide, and the smoke and a seawater-based absorbent enter a shell pass and a tube pass of the hydrophobic hollow fiber membrane absorber respectively; SO2 and NOX in the smoke and the seawater-based absorbent perform fast interface reaction through membrane wall micropores, and a reaction product is moved away timely, so that simultaneous desulphurization and denitration of the smoke are realized; and a desulphurized and denitrated absorption liquid is treated and discharged after the absorption liquid is up to the standard. According to the process, two phases of gas and liquid are not directly contacted, the flowing speed is independently controlled, the adjusting range is wide, and problems such as serious equipment corrosion, heavy metal pollution hidden danger and the like, which exist in a conventional seawater desulfurization process, can be avoided; and impact of smoke containing high-concentration pollutants can be flexibly coped with, the degree of automation is high, the operation and the maintenance are convenient and fast, and the device and the process are suitable for upgrading and reconstruction of boilers in a coastal area and other desulfurization and denitration processes which produce waste gas.

Description

technical field [0001] The invention belongs to the intersecting field of air pollution control technology and application of membrane science and technology, and specifically relates to a process for simultaneously removing sulfur dioxide and nitrogen oxides in flue gas in one process using membrane absorption technology and seawater-based absorbent. Background technique [0002] Sulfur dioxide and nitrogen oxides in the atmosphere mainly come from the combustion of fossil fuels such as industrial waste gas and coal and oil. In our country at present and for a long period of time in the future, it is still necessary to provide heat and power resources through coal combustion. [0003] Currently, industrialized SO 2 / NO X Most of the combined desulfurization process is desulfurization by limestone-gypsum flue gas desulfurization system first, and then denitrification by selective catalytic reduction denitrification technology (SCR). The desulfurization and denitrification ...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D53/60B01D53/22
CPCY02A50/20
Inventor 陈颖关毅鹏刘铮郭春刚刘国昌李浩李晓明李雪梅吕经烈
Owner TIANJIN SEA WATER DESALINATION & COMPLEX UTILIZATION INST STATE OCEANOGRAPHI
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