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Ammonia process for performing desulfurization and denitration on flue gas simultaneously

A technology for desulfurization and denitrification, flue gas, applied in separation methods, chemical instruments and methods, separation of dispersed particles, etc., can solve problems such as ammonia escape

Active Publication Date: 2011-09-21
SICHUAN JUNHE ENVIRONMENTAL PROTECTION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] The purpose of the present invention is to overcome the above defects, provide a process for simultaneous desulfurization and denitrification of ammonia in flue gas that can be applied industrially, solve the problem of ammonia escape in the absorption liquid, ensure the efficiency of denitrification and desulfurization, and by-products can be reused without producing New sources of pollution, the process has no strict requirements on equipment, low energy consumption, and economical and reasonable operation

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Flue gas to be treated, measured its SO 2 The content is 6000mg / Nm 3 , NO x The content is 800mg / Nm 3 , HCl content is 80mg / Nm 3 , soot content is 80mg / Nm 3 , Fe in soot 2 o 3 The mass fraction is 9.5%, the mass fraction of magnesium oxide is 3.5%, and the mass fraction of calcium oxide is 5.0%.

[0033] Configure the composition of the absorption liquid:

[0034] Cobalt ammonium complex, the mass fraction is 0.2%.

[0035] Free ammonia, mass fraction 1000PPM;

[0036] Chloride ion, the mass fraction is 2%;

[0037] The mass fraction of metal ions is 0.05-5%, wherein the mass fraction of magnesium ions is 0.1%, the mass fraction of calcium ions is 0.01%, the mass fraction of manganese ions is 0.2%, and the mass fraction of iron ions is 0.3%.

[0038] The desulfurization and denitrification process of this embodiment is carried out in a countercurrent spray purification empty tower. The spray tower is not easy to scale and block, and the pressure loss is small...

Embodiment 2

[0049] Flue gas to be treated, measured its SO 2 The content is 18000mg / Nm 3 , NO x The content is 1100mg / Nm 3 , HCl content is 175mg / Nm 3 , soot content is 370mg / Nm 3 , Fe in soot 2 o 3 The mass fraction is 7.5%, the mass fraction of magnesium oxide is 5.5%, and the mass fraction of calcium oxide is 7.5%.

[0050] Configure the absorption liquid, consisting of:

[0051] Cobalt ammonium complex, the mass fraction is 0.4%

[0052] Free ammonia, mass fraction 950PPM;

[0053] Chloride ion, mass fraction 5%;

[0054] The mass fraction of metal ions is 5%, among which the mass fraction of magnesium ions is 0.5%, the mass fraction of calcium ions is 0.02%, the mass fraction of manganese ions is 0.8%, and the mass fraction of iron ions is 1.4%.

[0055] The desulfurization and denitrification process of this embodiment is carried out in a countercurrent spray purification tower, the tower height is 30m, the tower inner diameter is 9m, the flue gas inlet is located in the ...

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PUM

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Abstract

The invention discloses an ammonia process for performing desulfurization and denitration on flue gas simultaneously. On the basis of ammonia process desulfurization and denitration and a complexing principle, the ammonia escape phenomenon of absorption liquid at each reaction stage is improved by adjusting the composition of the absorption liquid, the concentration of free ammonia in the absorption liquid is ensured, the circulation flow rate of the absorption liquid is reduced, denitration and desulfurization efficiency is improved, the flue gas purification effect is good, byproducts can be recycled, the environment is prevented from being polluted, the process can achieve an expected effect when applied to a denitration and desulfurization combined device and a denitration and desulfurization integrated device, industrial application can be truly realized, the process is more suitable to be realized by the denitration and desulfurization integrated device, and the effects of simplifying an equipment structure and reducing investment and energy consumption are achieved.

Description

technical field [0001] The invention relates to a process for flue gas desulfurization and denitrification, in particular to a process for simultaneously desulfurizing and denitrifying flue gas with ammonia. Background technique [0002] Boilers or thermal power plants that use coal or oil as fuel, and sintering machines in iron and steel plants that use iron ore as raw materials emit a large amount of flue gas. These flue gases contain harmful substances such as SOx, NOx, HCl and HF, among which sulfur oxides SOx (including SO2 and SO3) and nitrogen oxides NOx are the main substances that form acid rain. Depending on the type of coal burned, the SOx content is usually 300-5000ppmv (1000-15000mg / Nm 3 ), the NOx content of nitrogen oxides is usually 100-1000ppmv (300-3000mg / Nm 3 )between. However, the amount of flue gas discharged in the world is huge every year. In terms of coal-fired boilers, the steam scale ranges from 75T / h to 2500T / h, the capacity of generating units ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/86B01D53/96B01D53/60
Inventor 李乐军王漫
Owner SICHUAN JUNHE ENVIRONMENTAL PROTECTION
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