Wet denitration method for high-sulfur flue gas

A wet denitrification and flue gas technology is applied in the field of wet denitration of high-sulfur flue gas, which can solve the problems of limited promotion, corrosion, and high energy consumption of the SCR process, and achieve the effect of improving the denitration effect.

Pending Publication Date: 2022-01-07
CINF ENG CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Since sulfur combustion in non-ferrous smelting produces a large amount of sulfur dioxide and part of sulfur trioxide, the presence of sulfur makes the treatment of nitrogen oxides in flue gas particularly difficult
[0003] Using the SNCR process, there are two major problems in the reduction of nitrogen oxides by spraying ammonia into the denitrification temperature range of the metallurgical furnace: 1. Oxygen-enriched combustion leads to high oxygen content in the flue gas. reaction, the actual consumption of ammonia is much larger than the ammonia demand for only reducing nitrogen oxides, and the operating cost is greatly increased; 2. The excess ammonia injected into the system will combine with sulfur trio

Method used

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  • Wet denitration method for high-sulfur flue gas
  • Wet denitration method for high-sulfur flue gas
  • Wet denitration method for high-sulfur flue gas

Examples

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Effect test

Embodiment 1

[0055] 80000Nm produced by smelting furnace of lead system 3 / h high sulfur nitrogen oxide flue gas, SO 2 Concentration 14%, NO x Concentration 500mg / Nm 3 , fuming furnace produces 20000Nm 3 / h low sulfur nitrogen oxide flue gas, SO 2 Concentration 1%, NO x Concentration 100mg / Nm 3 . Flue gas NO after mixing x Concentration 420mg / Nm 3 (dry basis), SO 2 The concentration is 11.4%, which meets the SO of the systemic acid system 2 concentration.

[0056] Sulfuric acid purification adopts dynamic-fill-dynamic-two-stage electrostatic demisting process, and the NO in the flue gas 2 (NO 2 About NO x 10%) is mostly absorbed by the purified dilute acid, and the produced NO returns to the original flue gas, and the nitrate enters the waste acid. According to the monitoring concentration of nitrate, add hydrazine sulfate (hydrazine sulfate) to reduce nitrate into N according to the stoichiometric ratio 2 , to treat the nitrate nitrogen in the sewage acid in advance.

[00...

Embodiment 2

[0063] 80000Nm produced by zinc leaching slag smelting furnace 3 / h high sulfur nitrogen oxide flue gas, SO 2 Concentration 12%, NO x Concentration 500mg / Nm 3 .

[0064] Sulfuric acid purification adopts dynamic-fill-dynamic-two-stage electrostatic demisting process, and the NO in the flue gas 2 (NO 2 About NO x 10%) is mostly absorbed by the purified dilute acid, and the produced NO returns to the original flue gas, and the nitrate enters the waste acid. According to the monitoring concentration of nitrate, add appropriate amount of hydroxylammonium sulfate to reduce nitrate to N 2 , to treat the nitrate nitrogen in the sewage acid in advance.

[0065] The purified high-sulfur flue gas enters the drying tower for dehydration, and after drying, the flue gas is converted into SO 2 Flue gas conversion SO 3 (Conversion rate above 90%), while part of NO and O 2 NO 2 with N 2 o 3 . The converted flue gas enters the first absorption tower for denitrification reaction N...

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Abstract

The invention discloses a wet denitration method for high-sulfur flue gas. The method comprises the following steps of 1) purifying, 2) conducting conversion and absorption, (3) discharging gas, and 4) conducting acid production treatment. High-sulfur flue gas self-denitration is carried out by adopting the characteristics that a purified dilute acid aqueous solution absorbs part of nitrogen oxides and concentrated sulfuric acid, and sulfur trioxide reacts with the nitrogen oxides to generate nitroso sulfuric acid. Advanced treatment of nitrososulfuric acid and iron nitrososulfate in the concentrated sulfuric acid is focused, and nitrososulfuric acid and iron nitrososulfate are reduced into nitrogen, water and sulfuric acid or ferrous sulfate through a medicament, so that the final purposes of sulfuric acid wet denitration and no adverse byproducts are achieved, and a complete closed-loop process is formed. According to the denitration system disclosed by the invention, advanced treatment processes such as reduction and purification of nitrososulfuric acid or iron nitrososulfate are also added. Not only are NOHSO4 and Fe(NO)SO4 reduced completely, but also the adverse effect of excess of a small amount of reducing agent is eliminated thoroughly, and the production quality of sulfuric acid is not reduced practically.

Description

technical field [0001] The invention belongs to the technical field of environmental protection denitrification, and in particular relates to a method for wet denitrification of high-sulfur flue gas. Background technique [0002] Due to the presence of nitrogen and fuel coal during the smelting process, nitrogen oxides cannot be avoided. With oxygen-enriched smelting, nitrogen still exists in the combustion-supporting gas, but its content is reduced from 78% in the air to 30%, or even less, but oxygen-enriched smelting significantly increases the combustion temperature (above 1500°C), which is a thermal type. The main cause of nitrogen oxides. When coal is used as fuel in the smelting process, almost all organic nitrogen in coal is converted into fuel-type nitrogen oxides. The cumulative concentration of nitrogen oxides in the two forms is hundreds of mg / Nm 3 , even thousands of mg / Nm 3 . Since sulfur combustion in non-ferrous smelting produces a large amount of sulfur ...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D53/50B01D53/56C01B17/775C01B17/80C01B21/02C01G49/14
CPCB01D53/507B01D53/78B01D53/56C01B17/775C01B17/80C01B21/02C01G49/14B01D2258/0283
Inventor 朱智颖杨晓武袁爱武蔡旺吴桂荣
Owner CINF ENG CO LTD
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